From 014619ec3c327bfc5203b90b47050dec8d009601 Mon Sep 17 00:00:00 2001 From: David Jansen Date: Mon, 29 Jul 2024 14:46:32 +0000 Subject: [PATCH] Update 'docs' folder with issue1147_GenericBoiler and delete old branches. --- docs/issue1147_GenericBoiler/index.html | 1203 ++++- .../naming_violations.txt | 492 +- .../regression/Fluid/comparison-dymola.log | 1622 +++++++ .../errors.csv | 102 + .../lowerBound.csv | 105 + .../reference.csv | 102 + .../test.csv | 102 + .../upperBound.csv | 106 + .../errors.csv | 102 + .../lowerBound.csv | 29 + .../reference.csv | 102 + .../test.csv | 102 + .../upperBound.csv | 29 + .../errors.csv | 102 + .../lowerBound.csv | 106 + .../reference.csv | 102 + .../test.csv | 102 + .../upperBound.csv | 105 + .../errors.csv | 102 + .../lowerBound.csv | 105 + .../reference.csv | 102 + .../test.csv | 102 + .../upperBound.csv | 105 + .../errors.csv | 102 + .../lowerBound.csv | 33 + .../reference.csv | 102 + .../test.csv | 102 + .../upperBound.csv | 31 + .../errors.csv 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  • diff --git a/docs/issue1147_GenericBoiler/naming_violations.txt b/docs/issue1147_GenericBoiler/naming_violations.txt index cdc7a1f51f..7b54913924 100644 --- a/docs/issue1147_GenericBoiler/naming_violations.txt +++ b/docs/issue1147_GenericBoiler/naming_violations.txt @@ -1,88 +1,62 @@ -AixLib/Systems/ModularEnergySystems/ModularBoiler/Examples/ModularBoilerSimple.mo -1: Name 'k' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Integer k=2 "number of consumers"; - -2: Missing documentation, Name 'MediumWater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium, Water. Affected line: package MediumWater = AixLib.Media.Water; - -3: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: ModularBoiler modularBoiler( hasPump=true, QNom=50000, T_start=303.15, hasFeedback=false, use_tableData=true, redeclare function HeatingCurveFunction = AixLib.Controls.SetPoints.Functions.HeatingCurveFunction, dp_Valve(displayUnit="Pa") = 6000, use_HeaCur=false, Kv=10, energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial, redeclare package Medium = MediumWater) annotation (Placement(transformation(extent={{-34,-30},{26,30}}))); - -4: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sources.Boundary_pT bou( use_T_in=false, redeclare package Medium = MediumWater, T=293.15, nPorts=1) annotation (Placement(transformation(extent={{-96,-12},{-72,12}}))); - -5: Missing documentation, Name 'boilerControlBus' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boiler, Control. Affected line: AixLib.Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,52},{10,72}}))); - -6: Missing documentation. Affected line: Modelica.Blocks.Sources.Constant TFlowSet(k=273 + 60) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-86,40}))); - -7: Missing documentation. Affected line: Modelica.Blocks.Sources.BooleanConstant isOnSet(k=true) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-88,76}))); - -8: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.MixingVolumes.MixingVolume vol( redeclare package Medium = AixLib.Media.Water, T_start=323.15, m_flow_nominal=modularBoiler.m_flow_nominal, V=0.1, nPorts=2) annotation (Placement(transformation(extent={{64,0},{84,20}}))); - -9: Missing documentation, Name 'prescribedHeatFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: prescribed, Heat. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow prescribedHeatFlow annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=270, origin={64,40}))); - -10: Missing documentation, Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( amplitude=-5000, f=4/86400, offset=-25000) annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=0, origin={50,68}))); - -11: Missing documentation, Name 'sine1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine1( amplitude=5, f=4/86400, offset=278.15) annotation (Placement(transformation(extent={{-128,46},{-108,66}}))); - - -AixLib/Systems/ModularEnergySystems/ModularBoiler/Example/ModularBoilerFeedback.mo -1: Name 'k' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Integer k=2 "number of consumers"; - -2: Missing documentation, Name 'MediumWater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium, Water. Affected line: package MediumWater = AixLib.Media.Water; +AixLib/Fluid/BoilerCHP/BaseClasses/OffDesignOperation.mo +1: Missing documentation, Name 'Medium' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium. Affected line: package Medium=AixLib.Media.Water;Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-8,90},{12,110}}))); -3: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: ModularBoiler modularBoiler( hasPump=true, QNom=50000, kFeedBack=1, TiFeedBack=1, T_start=303.15, hasFeedback=true, use_tableData=true, redeclare function HeatingCurveFunction = AixLib.Controls.SetPoints.Functions.HeatingCurveFunction, dp_Valve(displayUnit="Pa") = 6000, use_HeaCur=false, Kv=10, energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial, redeclare package Medium = MediumWater) annotation (Placement(transformation(extent={{-34,-30},{26,30}}))); +2: Missing documentation. Affected line: Modelica.Blocks.Math.Add add2(k2=-1) annotation (Placement(transformation(extent={{-68,-26},{-50,-8}}))); -4: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sources.Boundary_pT bou( use_T_in=false, redeclare package Medium = MediumWater, T=293.15, nPorts=1) annotation (Placement(transformation(extent={{-96,-12},{-72,12}}))); +3: Missing documentation, Name 'devision1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: devision. Affected line: Modelica.Blocks.Math.Division devision1 annotation (Placement(transformation(extent={{-50,-64},{-30,-44}}))); -5: Missing documentation, Name 'boilerControlBus' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boiler, Control. Affected line: AixLib.Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,52},{10,72}}))); +4: Missing documentation, Name 'multiplex4' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: multiplex4. Affected line: Modelica.Blocks.Routing.Multiplex4 multiplex4 annotation (Placement(transformation(extent={{24,10},{46,32}}))); -6: Missing documentation. Affected line: Modelica.Blocks.Sources.Constant TFlowSet(k=273 + 60) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-86,40}))); +5: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: SDF.NDTable boilerEffciency( nin=4, readFromFile=true, filename=ModelicaServices.ExternalReferences.loadResource( "modelica://AixLib/Resources/Data/Fluid/BoilerCHP/BaseClasses/GenericBoiler/Boiler_Generic_Characteristic_Chart.sdf"), dataset="/Characteristic chart", dataUnit="-", scaleUnits={"K","K","-","-"}, interpMethod=SDF.Types.InterpolationMethod.Linear, extrapMethod=SDF.Types.ExtrapolationMethod.Hold) "Characteristic chart of adiabatic efficiency" annotation (Placement(transformation(extent={{60,12},{80,32}}))); -7: Missing documentation. Affected line: Modelica.Blocks.Sources.BooleanConstant isOnSet(k=true) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-88,76}))); +6: Missing documentation, Name 'devision' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: devision. Affected line: Modelica.Blocks.Math.Division devision annotation (Placement(transformation(extent={{-30,-30},{-12,-12}}))); -8: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.MixingVolumes.MixingVolume vol( redeclare package Medium = AixLib.Media.Water, T_start=323.15, m_flow_nominal=modularBoiler.m_flow_nominal, V=0.1, nPorts=2) annotation (Placement(transformation(extent={{64,0},{84,20}}))); +7: Missing documentation. Affected line: Modelica.Blocks.Math.Add add1(k1=-1) annotation (Placement(transformation(extent={{-32,14},{-12,34}}))); -9: Missing documentation, Name 'prescribedHeatFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: prescribed, Heat. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow prescribedHeatFlow annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=270, origin={64,40}))); +8: Missing documentation, Name 'm_flow_nom' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_flow_nom. Affected line: protected parameter Modelica.Units.SI.MassFlowRate m_flow_nom=QNom/(Medium.cp_const*( TSupNom - TRetNom)); -10: Missing documentation, Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( amplitude=-9000, f=4/86400, offset=-45000) annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=0, origin={50,68}))); -11: Missing documentation, Name 'sine1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine1( amplitude=5, f=4/86400, offset=278.15) annotation (Placement(transformation(extent={{-128,46},{-108,66}}))); +AixLib/Fluid/BoilerCHP/BaseClasses/DesignOperation.mo +1: Name 'ReturnTemp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Return, Temp. Affected line: Modelica.Blocks.Sources.RealExpression ReturnTemp(y=TRetNom) "Nominal return temperature" annotation (Placement(transformation(extent={{-100,6},{-54,30}}))); -12: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sensors.TemperatureTwoPort senTRet( redeclare final package Medium = AixLib.Media.Water, final m_flow_nominal=modularBoiler.m_flow_nominal, final initType=Modelica.Blocks.Types.Init.InitialState, final transferHeat=false, final m_flow_small=0.001) "Temperature sensor of cold side of heat generator (supply)" annotation ( Placement(transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={24,-62}))); +2: Name 'y_fullLoad' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: y_full, Load. Affected line: Modelica.Blocks.Sources.RealExpression y_fullLoad(y=1) "realtive power" annotation (Placement(transformation(extent={{-100,-52},{-54,-28}}))); +3: Name 'conductance' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: conductance. Affected line: Modelica.Blocks.Sources.RealExpression conductance(y=0.0465*QNom/1000 + 4.9891) "Thermal conductance" annotation (Placement(transformation(extent={{-98,54},{-52,78}}))); -AixLib/Fluid/BoilerCHP/CHPNoControl.mo -1: Name 'param' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: param. Affected line: parameter AixLib.DataBase.CHP.CHPDataSimple.CHPBaseDataDefinition param "CHP data set" annotation (choicesAllMatching=true, Dialog(group="Unit properties")); +4: Missing documentation, Name 'division' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: division. Affected line: Modelica.Blocks.Math.Division division annotation (Placement(transformation(extent={{58,48},{78,68}}))); -2: Name 'minCapacity' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Capacity. Affected line: parameter Real minCapacity = 0 "Minimum allowable working capacity (unit [-])" annotation(Dialog(group="Unit properties")); +5: Missing documentation, Name 'multiplex4' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: multiplex4. Affected line: Modelica.Blocks.Routing.Multiplex4 multiplex4 annotation (Placement(transformation(extent={{18,-16},{38,4}}))); -3: Name 'G' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance G=0.003*param.data_CHP[end, 3] /50 "Constant thermal conductance to environment(G=Q_loss/dT)"; +6: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: SDF.NDTable boilerEffciency( nin=4, readFromFile=true, filename=ModelicaServices.ExternalReferences.loadResource( "modelica://AixLib/Resources/Data/Fluid/BoilerCHP/BaseClasses/GenericBoiler/Boiler_Generic_Characteristic_Chart.sdf"), dataset="/Characteristic chart", dataUnit="-", scaleUnits={"K","K","-","-"}, interpMethod=SDF.Types.InterpolationMethod.Linear, extrapMethod=SDF.Types.ExtrapolationMethod.Hold) "Characteristic chart of adiabatic boiler efficiency" annotation (Placement(transformation(extent={{54,-16},{74,4}}))); -4: Name 'u_rel' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: u_rel. Affected line: Modelica.Blocks.Interfaces.RealInput u_rel( final unit="1") "Relative" annotation (Placement( transformation(extent={{-126,66},{-100,94}}, rotation=0), iconTransformation(extent={{-80,-70},{-60,-50}}))); +7: Missing documentation. Affected line: Modelica.Blocks.Math.Add add annotation (Placement(transformation(extent={{20,54},{40,74}}))); -5: Name 'electricalPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: electrical, Power. Affected line: Modelica.Blocks.Interfaces.RealOutput electricalPower( final quantity="Power", final unit="W") "Electrical power" annotation (Placement( transformation( origin={20,110}, extent={{-10,-10},{10,10}}, rotation=90), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={-50,90}))); +8: Missing documentation. Affected line: Modelica.Blocks.Math.Add add1(k1=-1) annotation (Placement(transformation(extent={{-36,-14},{-16,6}}))); -6: Name 'thermalPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: thermal, Power. Affected line: Modelica.Blocks.Interfaces.RealOutput thermalPower(final unit="W") "Thermal power" annotation (Placement( transformation( origin={36,110}, extent={{-10,-10},{10,10}}, rotation=90), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={-20,90}))); +9: Name 'SupplyTemp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Supply, Temp. Affected line: Modelica.Blocks.Sources.RealExpression SupplyTemp(y=TSupNom) "Nominal supply temperature" annotation (Placement(transformation(extent={{-100,-22},{-54,2}}))); -7: Name 'fuelInput' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fuel, Input. Affected line: Modelica.Blocks.Interfaces.RealOutput fuelInput(final unit="W") "Fuel input" annotation (Placement(transformation( origin={51,110}, extent={{-10,-11},{10,11}}, rotation=90), iconTransformation( extent={{-10,-11},{10,11}}, rotation=90, origin={20,90}))); +10: Name 'DeltaT_amb' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Delta, T_amb. Affected line: Modelica.Blocks.Sources.RealExpression DeltaT_amb(y=TSupNom - 293.15) "temperature difference supply-ambient" annotation (Placement(transformation(extent={{-100,80},{-54,104}}))); -8: Name 'fuelConsumption' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fuel, Consumption. Affected line: Modelica.Blocks.Interfaces.RealOutput fuelConsumption "Fuel consumption" annotation (Placement(transformation( origin={66,110}, extent={{-10,-10},{10,10}}, rotation=90), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={50,90}))); +11: Name 'losses' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: losses. Affected line: Modelica.Blocks.Math.Product losses "Nominal boiler losses" annotation (Placement(transformation(extent={{-32,76},{-12,96}}))); -9: Name 'combiTable1Ds' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: combi, Table, Ds. Affected line: Modelica.Blocks.Tables.CombiTable1Ds combiTable1Ds( tableName="NoName", fileName="NoName", final table=param.data_CHP) "Time table to read CHP performance data" annotation (Placement(transformation(extent={{40,40},{60,60}}, rotation=0))); -10: Name 'limiter' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: limiter. Affected line: Modelica.Blocks.Nonlinear.Limiter limiter(final uMax=1, final uMin= minCapacity) "Limits the rel power between 0 and 1" annotation (Placement(transformation(extent={{-60,40},{-40,60}}))); +AixLib/Fluid/Solar/Thermal/SolarThermal.mo +1: Name 'pressureDropCoeff' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: pressure, Drop, Coeff. Affected line: parameter Real pressureDropCoeff(unit="(Pa.s2)/m6") = 2500/(A*2.5e-5)^2 "Pressure drop coefficient, delta_p[Pa] = PD * Q_flow[m^3/s]^2"; -11: Name 'gain4' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: gain4. Affected line: Modelica.Blocks.Math.Gain gain4(final k=1000) "Conversion factor" annotation (Placement(transformation(extent={{4,-4},{-4,4}}, rotation=270, origin={66,90}))); +2: Name 'Collector' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Collector. Affected line: parameter AixLib.DataBase.SolarThermal.SolarThermalBaseDataDefinition Collector = AixLib.DataBase.SolarThermal.SimpleAbsorber() "Properties of Solar Thermal Collector" annotation(Dialog(group = "Efficienc"), choicesAllMatching = true); -12: Name 'gain3' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: gain3. Affected line: Modelica.Blocks.Math.Gain gain3(final k=1000) "Conversion factor" annotation (Placement(transformation(extent={{4,-4},{-4,4}}, rotation=270, origin={50,90}))); +3: Name 'T_air' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_air. Affected line: Modelica.Blocks.Interfaces.RealInput T_air( quantity="ThermodynamicTemperature", unit="K") "Outdoor air temperature in K" annotation(Placement(transformation(extent = {{-20, -20}, {20, 20}}, rotation = 270, origin={-60,100}))); -13: Name 'toPercent' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Percent. Affected line: Modelica.Blocks.Math.Gain toPercent(final k=100) "Conversion factor" annotation (Placement(transformation( extent={{6,-6},{-6,6}}, rotation=180, origin={12,50}))); +4: Name 'Irradiation' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Irradiation. Affected line: Modelica.Blocks.Interfaces.RealInput Irradiation( quantity="Irradiance", unit="W/m2") "Solar irradiation on a horizontal plane in W/m2" annotation(Placement(transformation(extent = {{-20, -20}, {20, 20}}, rotation = 270, origin={0,100}))); -14: Name 'internalCapacity' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: internal, Capacity. Affected line: Modelica.Thermal.HeatTransfer.Components.HeatCapacitor internalCapacity(final C=C, T(start=T_start)) "Boiler thermal capacity (dry weight)" annotation (Placement(transformation( extent={{-10,10},{10,-10}}, rotation=90, origin={2,-40}))); +5: Missing documentation, Name 'solarThermalEfficiency' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: solar, Thermal, Efficiency. Affected line: AixLib.Fluid.Solar.Thermal.BaseClasses.SolarThermalEfficiency solarThermalEfficiency(Collector=Collector) annotation (Placement(transformation(extent={{-70,32},{-34,68}}))); -15: Name 'ConductanceToEnv' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Conductance. Affected line: Modelica.Thermal.HeatTransfer.Components.ThermalConductor ConductanceToEnv(final G=G) "Thermal resistance of the boiler casing" annotation ( Placement(transformation( extent={{10,-10},{-10,10}}, rotation=180, origin={-30,-20}))); +6: Missing documentation, Name 'convertRelHeatFlow2absHeatFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: convert, Heat, Flow2abs, Heat. Affected line: Modelica.Blocks.Math.Gain convertRelHeatFlow2absHeatFlow(final k=A) annotation (Placement(transformation(extent={{-16,44},{-4,56}}))); -16: Name 'T_amb' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb. Affected line: Modelica.Thermal.HeatTransfer.Interfaces.HeatPort_b T_amb "Heat port for heat losses to ambient" annotation ( Placement(transformation(extent={{30,-30},{50,-10}}), iconTransformation( extent={{58,-60},{78,-40}}))); +7: Missing documentation, Name 'calcTempMean' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: calc, Temp, Mean. Affected line: Modelica.Blocks.Math.Add calcTempMean(k1=0.5, k2=0.5) annotation (Placement( transformation( extent={{-5,-5},{5,5}}, rotation=90, origin={-51,3}))); AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/DeviceStatusDelay.mo @@ -125,172 +99,88 @@ AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/DeviceStatusDelay.mo 19: Missing documentation, Name 'booleanExpression' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boolean, Expression. Affected line: Modelica.Blocks.Sources.BooleanExpression booleanExpression if not use_safetyShutoff annotation (Placement(transformation(extent={{-120,-66},{-100,-46}}))); -AixLib/Systems/ModularEnergySystems/ModularBoiler/Example/ModularBoilerHeatingCurve.mo -1: Name 'k' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Integer k=2 "number of consumers"; - -2: Missing documentation, Name 'MediumWater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium, Water. Affected line: package MediumWater = AixLib.Media.Water; - -3: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: ModularBoiler modularBoiler( hasPump=true, QNom=50000, T_start=303.15, hasFeedback=false, use_tableData=true, redeclare function HeatingCurveFunction = AixLib.Controls.SetPoints.Functions.HeatingCurveFunction, dp_Valve(displayUnit="Pa") = 6000, use_HeaCur=true, Kv=10, energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial, redeclare package Medium = MediumWater) annotation (Placement(transformation(extent={{-34,-30},{26,30}}))); - -4: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sources.Boundary_pT bou( use_T_in=false, redeclare package Medium = MediumWater, T=293.15, nPorts=1) annotation (Placement(transformation(extent={{-96,-12},{-72,12}}))); - -5: Missing documentation, Name 'boilerControlBus' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boiler, Control. Affected line: AixLib.Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,52},{10,72}}))); - -6: Missing documentation. Affected line: Modelica.Blocks.Sources.BooleanConstant isOnSet(k=true) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-88,76}))); - -7: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.MixingVolumes.MixingVolume vol( redeclare package Medium = AixLib.Media.Water, T_start=323.15, m_flow_nominal=modularBoiler.m_flow_nominal, V=0.1, nPorts=2) annotation (Placement(transformation(extent={{64,0},{84,20}}))); - -8: Missing documentation, Name 'prescribedHeatFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: prescribed, Heat. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow prescribedHeatFlow annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=270, origin={64,40}))); - -9: Missing documentation, Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( amplitude=-5000, f=4/86400, offset=-25000) annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=0, origin={50,68}))); - -10: Missing documentation, Name 'sine1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine1( amplitude=5, f=4/86400, offset=278.15) annotation (Placement(transformation(extent={{-128,46},{-108,66}}))); - - -AixLib/Systems/ModularEnergySystems/ModularBoiler/Examples/ModularBoilerFeedback.mo -1: Name 'k' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Integer k=2 "number of consumers"; - -2: Missing documentation, Name 'MediumWater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium, Water. Affected line: package MediumWater = AixLib.Media.Water; - -3: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: ModularBoiler modularBoiler( hasPump=true, QNom=50000, kFeedBack=1, TiFeedBack=1, T_start=303.15, hasFeedback=true, use_tableData=true, redeclare function HeatingCurveFunction = AixLib.Controls.SetPoints.Functions.HeatingCurveFunction, dp_Valve(displayUnit="Pa") = 6000, use_HeaCur=false, Kv=10, energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial, redeclare package Medium = MediumWater) annotation (Placement(transformation(extent={{-34,-30},{26,30}}))); - -4: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sources.Boundary_pT bou( use_T_in=false, redeclare package Medium = MediumWater, T=293.15, nPorts=1) annotation (Placement(transformation(extent={{-96,-12},{-72,12}}))); - -5: Missing documentation, Name 'boilerControlBus' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boiler, Control. Affected line: AixLib.Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,52},{10,72}}))); - -6: Missing documentation. Affected line: Modelica.Blocks.Sources.Constant TFlowSet(k=273 + 60) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-86,40}))); - -7: Missing documentation. Affected line: Modelica.Blocks.Sources.BooleanConstant isOnSet(k=true) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-88,76}))); - -8: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.MixingVolumes.MixingVolume vol( redeclare package Medium = AixLib.Media.Water, T_start=323.15, m_flow_nominal=modularBoiler.m_flow_nominal, V=0.1, nPorts=2) annotation (Placement(transformation(extent={{64,0},{84,20}}))); - -9: Missing documentation, Name 'prescribedHeatFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: prescribed, Heat. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow prescribedHeatFlow annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=270, origin={64,40}))); - -10: Missing documentation, Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( amplitude=-9000, f=4/86400, offset=-45000) annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=0, origin={50,68}))); - -11: Missing documentation, Name 'sine1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine1( amplitude=5, f=4/86400, offset=278.15) annotation (Placement(transformation(extent={{-128,46},{-108,66}}))); - -12: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sensors.TemperatureTwoPort senTRet( redeclare final package Medium = AixLib.Media.Water, final m_flow_nominal=modularBoiler.m_flow_nominal, final initType=Modelica.Blocks.Types.Init.InitialState, final transferHeat=false, final m_flow_small=0.001) "Temperature sensor of cold side of heat generator (supply)" annotation ( Placement(transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={24,-62}))); - - -AixLib/Systems/ModularEnergySystems/ModularBoiler/Example/ModularBoilerSimple.mo -1: Name 'k' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Integer k=2 "number of consumers"; - -2: Missing documentation, Name 'MediumWater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium, Water. Affected line: package MediumWater = AixLib.Media.Water; - -3: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: ModularBoiler modularBoiler( hasPump=true, QNom=50000, T_start=303.15, hasFeedback=false, use_tableData=true, redeclare function HeatingCurveFunction = AixLib.Controls.SetPoints.Functions.HeatingCurveFunction, dp_Valve(displayUnit="Pa") = 6000, use_HeaCur=false, Kv=10, energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial, redeclare package Medium = MediumWater) annotation (Placement(transformation(extent={{-34,-30},{26,30}}))); - -4: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sources.Boundary_pT bou( use_T_in=false, redeclare package Medium = MediumWater, T=293.15, nPorts=1) annotation (Placement(transformation(extent={{-96,-12},{-72,12}}))); - -5: Missing documentation, Name 'boilerControlBus' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boiler, Control. Affected line: AixLib.Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,52},{10,72}}))); - -6: Missing documentation. Affected line: Modelica.Blocks.Sources.Constant TFlowSet(k=273 + 60) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-86,40}))); - -7: Missing documentation. Affected line: Modelica.Blocks.Sources.BooleanConstant isOnSet(k=true) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-88,76}))); - -8: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.MixingVolumes.MixingVolume vol( redeclare package Medium = AixLib.Media.Water, T_start=323.15, m_flow_nominal=modularBoiler.m_flow_nominal, V=0.1, nPorts=2) annotation (Placement(transformation(extent={{64,0},{84,20}}))); - -9: Missing documentation, Name 'prescribedHeatFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: prescribed, Heat. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow prescribedHeatFlow annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=270, origin={64,40}))); - -10: Missing documentation, Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( amplitude=-5000, f=4/86400, offset=-25000) annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=0, origin={50,68}))); - -11: Missing documentation, Name 'sine1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine1( amplitude=5, f=4/86400, offset=278.15) annotation (Placement(transformation(extent={{-128,46},{-108,66}}))); - - -AixLib/Fluid/BoilerCHP/BaseClasses/PartialHeatGenerator.mo -1: Name 'transferHeat' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: transfer, Heat. Affected line: parameter Boolean transferHeat=false "If true, temperature T converges towards TAmb when no flow" annotation (Dialog(tab="Advanced", group="Sensor Properties")); - -2: Name 'm_flow_start' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_flow. Affected line: parameter Modelica.Units.SI.MassFlowRate m_flow_start=0 "Guess value of m_flow = port_a.m_flow" annotation (Dialog(tab="Initialization")); - -3: Name 'a' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: a. Affected line: parameter Real a "Coefficient of old approach from model Modelica.Fluid.Fittings.GenericResistances.VolumeFlowRate. Recalculated to dp_nominal based on IBPSA approach." annotation (Dialog(tab="Advanced", group="Pressure drop")); - -4: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Sensors.TemperatureTwoPort senTRet( redeclare final package Medium = Medium, final tau=tau, final m_flow_nominal=m_flow_nominal, final initType=initType, final T_start=T_start, final transferHeat=transferHeat, final TAmb=TAmb, final tauHeaTra=tauHeaTra, final allowFlowReversal=allowFlowReversal, final m_flow_small=m_flow_small) "Temperature sensor of cold side of heat generator (return)" annotation (Placement(transformation(extent={{-80,-90},{-60,-70}})));Sensors.TemperatureTwoPort senTSup( redeclare final package Medium = Medium, final tau=tau, final m_flow_nominal=m_flow_nominal, final initType=initType, final T_start=T_start, final transferHeat=transferHeat, final TAmb=TAmb, final tauHeaTra=tauHeaTra, final allowFlowReversal=allowFlowReversal, final m_flow_small=m_flow_small) "Temperature sensor of hot side of heat generator (supply)" annotation (Placement(transformation(extent={{30,-90},{50,-70}})));Sensors.MassFlowRate senMasFlo( redeclare final package Medium = Medium, final allowFlowReversal=allowFlowReversal) "Sensor for mass flwo rate" annotation (Placement(transformation(extent={{60,-90},{80,-70}}))); - -5: Name 'heater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heater. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow heater "Prescribed heat flow" annotation ( Placement(transformation( extent={{-10,-10},{10,10}}, rotation=-90, origin={-60,-50}))); - -6: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: MixingVolumes.MixingVolume vol( redeclare final package Medium = Medium, final m_flow_nominal=m_flow_nominal, final m_flow_small=m_flow_small, final allowFlowReversal=allowFlowReversal, final nPorts=2, final p_start=p_start, final T_start=T_start) "Fluid volume" annotation (Placement(transformation(extent={{-50,-80},{-30,-60}})));FixedResistances.PressureDrop preDro( redeclare final package Medium = Medium, final m_flow_nominal=m_flow_nominal, final show_T=false, final allowFlowReversal=allowFlowReversal, final dp_nominal=dp_nominal) "Pressure drop" annotation (Placement(transformation(extent={{-20,-90},{0,-70}}))); - -7: Name 'rho_default' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: rho_default. Affected line: final parameter Modelica.Units.SI.Density rho_default=Medium.density_pTX( Medium.p_default, Medium.T_default, Medium.X_default) "Density used for parameterization of pressure curve" annotation (Dialog(tab="Advanced", group="Pressure drop")); +AixLib/Fluid/BoilerCHP/BoilerGeneric.mo +1: Name 'internalCapacity' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: internal, Capacity. Affected line: Modelica.Thermal.HeatTransfer.Components.HeatCapacitor internalCapacity(final C=C, T(start=T_start)) "Boiler thermal capacity (dry weight)" annotation (Placement(transformation( extent={{-10,10},{10,-10}}, rotation=90, origin={-18,-50}))); +2: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: BaseClasses.OffDesignOperation offDesignOperation( QNom=QNom, TSupNom=TSupNom, TRetNom=TRetNom) "off design operation" annotation (Placement(transformation(extent={{30,70},{50,90}}))); -AixLib/Fluid/BoilerCHP/BoilerNoControl.mo -1: Name 'paramBoiler' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: param, Boiler. Affected line: parameter AixLib.DataBase.Boiler.General.BoilerTwoPointBaseDataDefinition paramBoiler "Parameters for Boiler" annotation (Dialog(tab="General", group= "Boiler type"), choicesAllMatching=true); +3: Name 'conductanceToEnv' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: conductance. Affected line: Modelica.Thermal.HeatTransfer.Components.ThermalConductor conductanceToEnv(final G= 0.0465*QNom/1000 + 4.9891) "Thermal resistance of the boiler casing" annotation (Placement(transformation( extent={{6,-6},{-6,6}}, rotation=180, origin={-38,-34}))); -2: Name 'G' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance G=0.003*Q_nom/50 "Constant thermal conductance to environment(G=Q_loss/dT)"; +4: Name 'fixedTemperature' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fixed, Temperature. Affected line: Modelica.Thermal.HeatTransfer.Sources.FixedTemperature fixedTemperature(T( displayUnit="K") = 293.15) "Temperature of environment around the boiler to account for heat losses" annotation (Placement(transformation(extent={{14,-40},{2,-28}}))); -3: Name 'Q_nom' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Q_nom. Affected line: parameter Modelica.Units.SI.Power Q_nom=paramBoiler.Q_nom "Nominal heating power"; +5: Missing documentation, Name 'heatFlowSensor' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Sensor. Affected line: Modelica.Thermal.HeatTransfer.Sensors.HeatFlowSensor heatFlowSensor annotation (Placement(transformation(extent={{-26,-28},{-14,-40}}))); -4: Name 'internalCapacity' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: internal, Capacity. Affected line: Modelica.Thermal.HeatTransfer.Components.HeatCapacitor internalCapacity( final C=C, T(start=T_start)) "Boiler thermal capacity (dry weight)" annotation (Placement(transformation( extent={{-10,10},{10,-10}}, rotation=90, origin={2,-40}))); +6: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,90},{10,110}}))); -5: Name 'ConductanceToEnv' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Conductance. Affected line: Modelica.Thermal.HeatTransfer.Components.ThermalConductor ConductanceToEnv( final G=G) "Thermal resistance of the boiler casing" annotation ( Placement(transformation( extent={{10,-10},{-10,10}}, rotation=180, origin={-30,-20}))); +7: Documentation too short, Name 'temperatureSensor' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: temperature, Sensor. Affected line: Modelica.Thermal.HeatTransfer.Sensors.TemperatureSensor temperatureSensor( final T(unit="K")) annotation (Placement(transformation(extent={{-50,-26},{-30,-6}}))); -6: Name 'QgasCalculation' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Qgas, Calculation. Affected line: Modelica.Blocks.Math.Product QgasCalculation "Calculate gas usage" annotation (Placement(transformation(extent={{-20,80},{0,100}}))); +8: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: BaseClasses.DesignOperation designOperation( QNom=QNom, TSupNom=TSupNom, TRetNom=TRetNom) "designOperation for design fuel power" annotation (Placement(transformation(extent={{-60,70},{-40,90}}))); -7: Name 'limiter' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: limiter. Affected line: Modelica.Blocks.Nonlinear.Limiter limiter(final uMax=1, final uMin=0) "Limits the rel power between 0 and 1" annotation (Placement(transformation(extent={{-80,60},{-60,80}}))); +9: Name 'fuelPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fuel, Power. Affected line: Modelica.Blocks.Math.Product fuelPower(final y(unit="W")) "fuel power" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=-90, origin={-44,48}))); -8: Name 'NominalGasConsumption' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Nominal, Consumption. Affected line: Modelica.Blocks.Sources.RealExpression NominalGasConsumption(final y=Q_nom/ max(etaLoadBased[:,2]*max(etaTempBased[:,2]))) "Nominal gas power" annotation (Placement(transformation(extent={{-62,88},{-34,104}}))); +10: Name 'thermalPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: thermal, Power. Affected line: Modelica.Blocks.Math.Product thermalPower(final y(unit="W")) "thermal power" annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=-90, origin={-38,14}))); -9: Name 'fuelPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fuel, Power. Affected line: Modelica.Blocks.Interfaces.RealOutput fuelPower "Connector of Real output signal" annotation (Placement(transformation( extent={{100,90},{120,110}}), iconTransformation(extent={{-10,-10},{10, 10}}, rotation=0, origin={72,110}))); +11: Name 'coeffPresLoss' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: coeff, Pres, Loss. Affected line: protected parameter Real coeffPresLoss=7.143*10^8*exp(-0.007078*QNom/1000) "Pressure loss coefficient of the heat generator"; -10: Name 'thermalPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: thermal, Power. Affected line: Modelica.Blocks.Interfaces.RealOutput thermalPower "Value of Real output" annotation (Placement(transformation(extent={{100,70},{120,90}}), iconTransformation(extent={{62,74},{82,94}}))); -11: Name 'u_rel' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: u_rel. Affected line: Modelica.Blocks.Interfaces.RealInput u_rel "Relative gas power [0,1]" annotation (Placement(transformation( extent={{-20,-20},{20,20}}, rotation=270, origin={-80,120}), iconTransformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-70,70}))); +AixLib/Fluid/BoilerCHP/Boiler.mo +1: Name 'paramBoiler' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: param, Boiler. Affected line: parameter AixLib.DataBase.Boiler.General.BoilerTwoPointBaseDataDefinition paramBoiler "Parameters for Boiler" annotation (Dialog(tab = "General", group = "Boiler type"), choicesAllMatching = true); -12: Name 'T_amb' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb. Affected line: Modelica.Thermal.HeatTransfer.Interfaces.HeatPort_b T_amb "Heat port for heat losses to ambient" annotation ( Placement(transformation(extent={{30,-30},{50,-10}}), iconTransformation( extent={{58,-60},{78,-40}}))); +2: Name 'paramHC' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: param. Affected line: parameter AixLib.DataBase.Boiler.DayNightMode.HeatingCurvesDayNightBaseDataDefinition paramHC "Parameters for heating curve" annotation (Dialog(group="Heating curves"), choicesAllMatching=true); -13: Name 'efficiencyTableLoadDepending' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: efficiency, Table, Load, Depending. Affected line: Modelica.Blocks.Tables.CombiTable1Dv efficiencyTableLoadDepending( final tableOnFile=false, final table=etaLoadBased, final columns={2}, final smoothness=Modelica.Blocks.Types.Smoothness.ContinuousDerivative) "Table with efficiency parameters" annotation (Placement(transformation(extent={{-40,50},{-19,71}}))); +3: Name 'KR' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: K. Affected line: parameter Real KR=1 "Gain of Boiler heater" annotation (Dialog(tab = "General", group = "Boiler type")); -14: Name 'QflowCalculation' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Qflow, Calculation. Affected line: Modelica.Blocks.Math.Product QflowCalculation "Calculation of the produced heatflow" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-60,2}))); +4: Name 'TN' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N. Affected line: parameter Modelica.Units.SI.Time TN=0.1 "Time Constant of boiler heater (T>0 required)" annotation (Dialog(tab="General", group="Boiler type")); -15: Name 'etaLoadBased' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Load, Based. Affected line: parameter Real etaLoadBased[:,2]=paramBoiler.eta "Table matrix for part load based efficiency (e.g. [0,0.99; 0.5, 0.98; 1, 0,97])"; +5: Name 'riseTime' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: rise. Affected line: parameter Modelica.Units.SI.Time riseTime=30 "Rise/Fall time for step input(T>0 required)" annotation (Dialog(tab="General", group="Boiler type")); -16: Name 'etaTempBased' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Temp, Based. Affected line: parameter Real etaTempBased[:,2]=[293.15,1.09; 303.15,1.08; 313.15,1.05; 323.15,1.; 373.15,0.99] "Table matrix for temperature based efficiency"; +6: Name 'declination' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: declination. Affected line: parameter Real declination=1.1 "Declination" annotation(Dialog(tab="External Control")); -17: Name 'etaCalculation' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Calculation. Affected line: Modelica.Blocks.Math.Product etaCalculation "calculates the efficiency of the boiler" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={10,50}))); +7: Name 'Tdelta_Max' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Tdelta_. Affected line: parameter Modelica.Units.SI.TemperatureDifference Tdelta_Max=2 "Difference from set flow temperature over which boiler stops" annotation (Dialog(tab="External Control")); -18: Name 'efficiencyTableLoadDepending1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: efficiency, Table, Load, Depending. Affected line: Modelica.Blocks.Tables.CombiTable1Dv efficiencyTableLoadDepending1( final tableOnFile=false, final table=etaTempBased, final columns={2}, final smoothness=Modelica.Blocks.Types.Smoothness.ContinuousDerivative) "Table with efficiency parameters" annotation (Placement(transformation(extent={{-40,20},{-19,41}}))); +8: Name 'Tdelta_Min' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Tdelta_. Affected line: parameter Modelica.Units.SI.TemperatureDifference Tdelta_Min=2 "Difference from set flow temperature under which boiler starts" annotation (Dialog(tab="External Control")); +9: Name 'Fb' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Fb. Affected line: parameter Modelica.Units.SI.Time Fb=3600 "Period of time for increased set temperature" annotation (Dialog(tab="External Control")); -AixLib/Fluid/Solar/Thermal/SolarThermal.mo -1: Name 'pressureDropCoeff' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: pressure, Drop, Coeff. Affected line: parameter Real pressureDropCoeff(unit="(Pa.s2)/m6") = 2500/(A*2.5e-5)^2 "Pressure drop coefficient, delta_p[Pa] = PD * Q_flow[m^3/s]^2"; +10: Name 'FA' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: F. Affected line: parameter Real FA=0.2 "Increment for increased set temperature" annotation(Dialog(tab="External Control")); -2: Name 'Collector' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Collector. Affected line: parameter AixLib.DataBase.SolarThermal.SolarThermalBaseDataDefinition Collector = AixLib.DataBase.SolarThermal.SimpleAbsorber() "Properties of Solar Thermal Collector" annotation(Dialog(group = "Efficienc"), choicesAllMatching = true); +11: Name 'TAmbient' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ambient. Affected line: Modelica.Blocks.Interfaces.RealInput TAmbient( final quantity="ThermodynamicTemperature", final unit="K", displayUnit="degC") "Ambient air temperature" annotation (Placement( transformation(extent={{-100,40},{-60,80}}), iconTransformation(extent= {{-80,60},{-60,80}}))); -3: Name 'T_air' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_air. Affected line: Modelica.Blocks.Interfaces.RealInput T_air( quantity="ThermodynamicTemperature", unit="K") "Outdoor air temperature in K" annotation(Placement(transformation(extent = {{-20, -20}, {20, 20}}, rotation = 270, origin={-60,100}))); +12: Name 'switchToNightMode' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: switch, Night, Mode. Affected line: Modelica.Blocks.Interfaces.BooleanInput switchToNightMode "Connector of Boolean input signal" annotation (Placement(transformation( extent={{-100,10},{-60,50}}), iconTransformation(extent={{-80,30},{-60, 50}}))); -4: Name 'Irradiation' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Irradiation. Affected line: Modelica.Blocks.Interfaces.RealInput Irradiation( quantity="Irradiance", unit="W/m2") "Solar irradiation on a horizontal plane in W/m2" annotation(Placement(transformation(extent = {{-20, -20}, {20, 20}}, rotation = 270, origin={0,100}))); +13: Name 'ExtControl' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Control. Affected line: replaceable model ExtControl = AixLib.Fluid.BoilerCHP.BaseClasses.Controllers.ExternalControlNightDayHC constrainedby AixLib.Fluid.BoilerCHP.BaseClasses.Controllers.PartialExternalControl "External control" annotation (Dialog(tab="External Control"),choicesAllMatching=true); -5: Missing documentation, Name 'solarThermalEfficiency' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: solar, Thermal, Efficiency. Affected line: AixLib.Fluid.Solar.Thermal.BaseClasses.SolarThermalEfficiency solarThermalEfficiency(Collector=Collector) annotation (Placement(transformation(extent={{-70,32},{-34,68}}))); -6: Missing documentation, Name 'convertRelHeatFlow2absHeatFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: convert, Heat, Flow2abs, Heat. Affected line: Modelica.Blocks.Math.Gain convertRelHeatFlow2absHeatFlow(final k=A) annotation (Placement(transformation(extent={{-16,44},{-4,56}}))); +AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/BoilerControl.mo +1: Name 'TReturnNom' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Return. Affected line: parameter Modelica.Units.SI.Temperature TReturnNom=323.15 "Nominal return temperature" annotation (Dialog(group="Nominal Condition")); -7: Missing documentation, Name 'calcTempMean' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: calc, Temp, Mean. Affected line: Modelica.Blocks.Math.Add calcTempMean(k1=0.5, k2=0.5) annotation (Placement( transformation( extent={{-5,-5},{5,5}}, rotation=90, origin={-51,3}))); +2: Name 'kFloTem' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Real kFloTem=1 "Gain of controller" annotation (Dialog(group= "Flow Temperature Control")); +3: Name 'TiFloTem' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ti. Affected line: parameter Modelica.Units.SI.Time TiFloTem=10 "Time constant of Integrator block" annotation (Dialog(group= "Flow Temperature Control")); -AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/InternalFirRatControl.mo -1: Name 'Ti' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ti. Affected line: parameter Modelica.Units.SI.Time Ti=10 "Time constant of Integrator block" annotation (Dialog(group="Flow Temperature PI")); +4: Name 'use_tableData' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: use_table, Data. Affected line: parameter Boolean use_tableData=true "Choose between tables or function to calculate TSet" annotation (Dialog(group="Heating Curve")); -2: Documentation too short. Affected line: Modelica.Blocks.Interfaces.RealInput TFlowMea(unit="K") annotation (Placement( transformation( extent={{-20,-20},{20,20}}, rotation=0, origin={-120,-52}))); +5: Missing documentation, Name 'HeatingCurveFunction' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heating, Curve, Function. Affected line: replaceable function HeatingCurveFunction = AixLib.Controls.SetPoints.Functions.HeatingCurveFunction annotation ( choicesAllMatching=true, Dialog(group="Heating Curve")); -3: Missing documentation. Affected line: Modelica.Blocks.Interfaces.RealOutput FirRatSet annotation (Placement(transformation(extent={{100,-10},{120,10}}))); +6: Missing documentation, Name 'declination' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: declination. Affected line: parameter Real declination=1 annotation (Dialog(group="Heating Curve")); +7: Missing documentation, Name 'day_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: day_hour. Affected line: parameter Real day_hour=6 annotation (Dialog(group="Heating Curve")); -AixLib/Fluid/BoilerCHP/BaseClasses/OffDesignOperation.mo -1: Missing documentation, Name 'Medium' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium. Affected line: package Medium=AixLib.Media.Water;Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-8,90},{12,110}}))); +8: Missing documentation, Name 'night_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: night_hour. Affected line: parameter Real night_hour=22 annotation (Dialog(group="Heating Curve")); -2: Missing documentation. Affected line: Modelica.Blocks.Math.Add add2(k2=-1) annotation (Placement(transformation(extent={{-68,-26},{-50,-8}}))); +9: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter Utilities.Time.Types.ZeroTime zerTim=AixLib.Utilities.Time.Types.ZeroTime.NY2017 "Enumeration for choosing how reference time (time = 0) should be defined. Used for heating curve" annotation (Dialog(group="Heating Curve")); -3: Missing documentation, Name 'devision1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: devision. Affected line: Modelica.Blocks.Math.Division devision1 annotation (Placement(transformation(extent={{-50,-64},{-30,-44}}))); +10: Name 'TOffset' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Offset. Affected line: parameter Modelica.Units.SI.ThermodynamicTemperature TOffset=0 "Offset to heating curve temperature" annotation (Dialog(group="Heating Curve")); -4: Missing documentation, Name 'multiplex4' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: multiplex4. Affected line: Modelica.Blocks.Routing.Multiplex4 multiplex4 annotation (Placement(transformation(extent={{24,10},{46,32}}))); +11: Name 'kFeedBack' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k, Feed, Back. Affected line: parameter Real kFeedBack=1 "Gain of controller" annotation (Dialog(group="Feedback Return Control")); -5: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: SDF.NDTable boilerEffciency( nin=4, readFromFile=true, filename=ModelicaServices.ExternalReferences.loadResource( "modelica://AixLib/Resources/Data/Fluid/BoilerCHP/BaseClasses/GenericBoiler/Boiler_Generic_Characteristic_Chart.sdf"), dataset="/Characteristic chart", dataUnit="-", scaleUnits={"K","K","-","-"}, interpMethod=SDF.Types.InterpolationMethod.Linear, extrapMethod=SDF.Types.ExtrapolationMethod.Hold) "Characteristic chart of adiabatic efficiency" annotation (Placement(transformation(extent={{60,12},{80,32}}))); +12: Name 'TiFeedBack' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ti, Feed, Back. Affected line: parameter Modelica.Units.SI.Time TiFeedBack=0.5 "Time constant of Integrator block" annotation (Dialog(group= "Feedback Return Control")); -6: Missing documentation, Name 'devision' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: devision. Affected line: Modelica.Blocks.Math.Division devision annotation (Placement(transformation(extent={{-30,-30},{-12,-12}}))); +13: Name 'yMaxFeedBack' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Feed, Back. Affected line: parameter Real yMaxFeedBack=0.99 "Upper limit of output" annotation (Dialog(group="Feedback Return Control")); -7: Missing documentation. Affected line: Modelica.Blocks.Math.Add add1(k1=-1) annotation (Placement(transformation(extent={{-32,14},{-12,34}}))); +14: Name 'yMinFeedBack' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Feed, Back. Affected line: parameter Real yMinFeedBack=0 "Lower limit of output" annotation (Dialog(group="Feedback Return Control")); -8: Missing documentation, Name 'm_flow_nom' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_flow_nom. Affected line: protected parameter Modelica.Units.SI.MassFlowRate m_flow_nom=QNom/(Medium.cp_const*( TSupNom - TRetNom)); +15: Missing documentation, Name 'boilerControlBus' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boiler, Control. Affected line: AixLib.Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,90},{10,110}}))); AixLib/Systems/ModularEnergySystems/ModularBoiler/Examples/ModularBoilerHeatingCurve.mo @@ -315,26 +205,6 @@ AixLib/Systems/ModularEnergySystems/ModularBoiler/Examples/ModularBoilerHeatingC 10: Missing documentation, Name 'sine1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine1( amplitude=5, f=4/86400, offset=278.15) annotation (Placement(transformation(extent={{-128,46},{-108,66}}))); -AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/SafetyControl.mo -1: Missing documentation. Affected line: Modelica.Blocks.Sources.RealExpression TFlowMaxExp(final y=TFlowMax) annotation (Placement(transformation(extent={{-96,-30},{-76,-10}}))); - -2: Missing documentation, Name 'greater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: greater. Affected line: Modelica.Blocks.Logical.Greater greater annotation (Placement(transformation(extent={{-48,-10},{-28,10}}))); - - -AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/heatingCurve.mo -1: Name 'use_tableData' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: use_table, Data. Affected line: parameter Boolean use_tableData=true "Choose between tables or function to calculate TSet" annotation (Dialog(group="Heating Curve")); - -2: Missing documentation, Name 'declination' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: declination. Affected line: parameter Real declination=1 annotation (Dialog(group="Heating Curve")); - -3: Missing documentation, Name 'day_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: day_hour. Affected line: parameter Real day_hour=6 annotation (Dialog(group="Heating Curve")); - -4: Missing documentation, Name 'night_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: night_hour. Affected line: parameter Real night_hour=22 annotation (Dialog(group="Heating Curve")); - -5: Name 'TOffset' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Offset. Affected line: parameter Modelica.Units.SI.ThermodynamicTemperature TOffset=0 "Offset to heating curve temperature" annotation (Dialog(group="Heating Curve")); - -6: Missing documentation, Name 'heatingCurve' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heating, Curve. Affected line: AixLib.Controls.SetPoints.HeatingCurve heatingCurve( final TOffset=TOffset, final use_dynTRoom=false, final zerTim=zerTim, final day_hour=day_hour, final night_hour=night_hour, final heatingCurveRecord= AixLib.DataBase.Boiler.DayNightMode.HeatingCurves_Vitotronic_Day23_Night10(), final declination=declination, redeclare function HeatingCurveFunction = HeatingCurveFunction, final use_tableData=use_tableData, final TRoom_nominal=293.15) annotation (Placement(transformation(extent={{-10,-10},{10,10}}))); - - AixLib/Systems/ModularEnergySystems/ModularBoiler/ModularBoiler.mo 1: Name 'MediumWater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium, Water. Affected line: package MediumWater = AixLib.Media.Water "Boiler Medium" annotation(Dialog(group="System setup")); @@ -387,164 +257,178 @@ AixLib/Systems/ModularEnergySystems/ModularBoiler/ModularBoiler.mo 25: Missing documentation, Name 'cp_medium' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: cp_medium. Affected line: parameter Modelica.Units.SI.SpecificHeatCapacity cp_medium = Medium.cp_const; -AixLib/Fluid/BoilerCHP/HeatGeneratorNoControl.mo -1: Name 'TCold' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Cold. Affected line: Modelica.Blocks.Interfaces.RealOutput TCold( final quantity="ThermodynamicTemperature", final unit="K", displayUnit="degC") "Temperature of the passing fluid" annotation (Placement(transformation(extent={{44,76},{64,96}}), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={-40,90}))); +AixLib/Fluid/BoilerCHP/Examples/BoilerGeneric.mo +1: Missing documentation, Name 'Medium' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium. Affected line: package Medium = AixLib.Media.Water annotation (choicesAllMatching=true); -2: Name 'massFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: mass. Affected line: Modelica.Blocks.Interfaces.RealOutput massFlow(quantity="MassFlowRate", final unit="kg/s") "Mass flow rate from port_a to port_b" annotation (Placement(transformation(extent={{100,30},{120,50}}), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={40,90}))); +2: Missing documentation. Affected line: AixLib.Fluid.BoilerCHP.BoilerGeneric boiGen( redeclare package Medium = Medium, T_start=293.15, QNom=20000, TSupNom=353.15, TRetNom=333.15) annotation (Placement(transformation(extent={{-8,-10},{12,10}}))); -3: Name 'coeffPresLoss' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: coeff, Pres, Loss. Affected line: parameter Real coeffPresLoss "Pressure loss coefficient of the heat generator"; +3: Name 'source' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: source. Affected line: Modelica.Fluid.Sources.MassFlowSource_T source( use_m_flow_in=false, redeclare package Medium = Medium, use_T_in=true, m_flow=20/4.18/20, T=313.15, nPorts=1) "Source" annotation (Placement(transformation(extent={{-62,-10},{-42,10}}))); +4: Name 'ramp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: ramp. Affected line: Modelica.Blocks.Sources.Ramp ramp( height=40, duration=500, offset=293.15, startTime=60) "Return temperature" annotation (Placement(transformation(extent={{-100,-6},{-80,14}}))); -AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/FeedbackControl.mo -1: Missing documentation, Name 'PIValve' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Valve. Affected line: public Modelica.Blocks.Continuous.LimPID PIValve( final controllerType=Modelica.Blocks.Types.SimpleController.PI, final k=k, final Ti=Ti, final yMax=yMax, final yMin=yMin, initType=Modelica.Blocks.Types.Init.InitialOutput, y_start=yMin) annotation (Placement(transformation( extent={{10,10},{-10,-10}}, rotation=180, origin={-2,0}))); +5: Documentation too short, Name 'sink' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sink. Affected line: Modelica.Fluid.Sources.Boundary_pT sink(nPorts=1, redeclare package Medium = Medium) "Sink" annotation (Placement(transformation(extent={{68,-10},{48,10}}))); -2: Name 'yValve' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Valve. Affected line: Modelica.Blocks.Interfaces.RealOutput yValve "Position of feedback valve" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={110,0}))); +6: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Controls.Continuous.LimPID conPID(u_m(unit="K"), controllerType=Modelica.Blocks.Types.SimpleController.PI, k=1, Ti=5, Td=1, yMax=1, yMin=0) annotation (Placement(transformation(extent={{-44,58},{-24,78}}))); -3: Name 'TReturnMea' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Return. Affected line: Modelica.Blocks.Interfaces.RealInput TReturnMea(unit="K") "Measured return temperature" annotation (Placement(transformation(extent={{-122,-20},{-82,20}}))); +7: Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( amplitude=5, f=100/(3600*24), phase=0, offset=273.15 + 75, startTime=700) "Ambient air temperature" annotation (Placement(transformation(extent={{-100,58},{-80,78}}))); -4: Missing documentation. Affected line: Modelica.Blocks.Math.Gain gain1(final k=-1) annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=0, origin={-34,0}))); -5: Missing documentation. Affected line: Modelica.Blocks.Math.Gain gain2(final k=-1) annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=0, origin={-68,-34}))); +AixLib/Systems/ModularEnergySystems/ModularBoiler/Examples/ModularBoilerFeedback.mo +1: Name 'k' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Integer k=2 "number of consumers"; -6: Name 'k' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Real k=1 "Gain of controller" annotation (Dialog(group="Feedback Return Control")); +2: Missing documentation, Name 'MediumWater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium, Water. Affected line: package MediumWater = AixLib.Media.Water; -7: Name 'Ti' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ti. Affected line: parameter Modelica.Units.SI.Time Ti=0.5 "Time constant of Integrator block" annotation (Dialog(group="Feedback Return Control")); +3: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: ModularBoiler modularBoiler( hasPump=true, QNom=50000, kFeedBack=1, TiFeedBack=1, T_start=303.15, hasFeedback=true, use_tableData=true, redeclare function HeatingCurveFunction = AixLib.Controls.SetPoints.Functions.HeatingCurveFunction, dp_Valve(displayUnit="Pa") = 6000, use_HeaCur=false, Kv=10, energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial, redeclare package Medium = MediumWater) annotation (Placement(transformation(extent={{-34,-30},{26,30}}))); +4: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sources.Boundary_pT bou( use_T_in=false, redeclare package Medium = MediumWater, T=293.15, nPorts=1) annotation (Placement(transformation(extent={{-96,-12},{-72,12}}))); -AixLib/Fluid/BoilerCHP/Examples/BoilerGeneric.mo -1: Missing documentation, Name 'Medium' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium. Affected line: package Medium = AixLib.Media.Water annotation (choicesAllMatching=true); +5: Missing documentation, Name 'boilerControlBus' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boiler, Control. Affected line: AixLib.Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,52},{10,72}}))); -2: Missing documentation. Affected line: AixLib.Fluid.BoilerCHP.BoilerGeneric boiGen( redeclare package Medium = Medium, T_start=293.15, QNom=20000, TSupNom=353.15, TRetNom=333.15) annotation (Placement(transformation(extent={{-8,-10},{12,10}}))); +6: Missing documentation. Affected line: Modelica.Blocks.Sources.Constant TFlowSet(k=273 + 60) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-86,40}))); -3: Name 'source' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: source. Affected line: Modelica.Fluid.Sources.MassFlowSource_T source( use_m_flow_in=false, redeclare package Medium = Medium, use_T_in=true, m_flow=20/4.18/20, T=313.15, nPorts=1) "Source" annotation (Placement(transformation(extent={{-62,-10},{-42,10}}))); +7: Missing documentation. Affected line: Modelica.Blocks.Sources.BooleanConstant isOnSet(k=true) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-88,76}))); -4: Name 'ramp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: ramp. Affected line: Modelica.Blocks.Sources.Ramp ramp( height=40, duration=500, offset=293.15, startTime=60) "Return temperature" annotation (Placement(transformation(extent={{-100,-6},{-80,14}}))); +8: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.MixingVolumes.MixingVolume vol( redeclare package Medium = AixLib.Media.Water, T_start=323.15, m_flow_nominal=modularBoiler.m_flow_nominal, V=0.1, nPorts=2) annotation (Placement(transformation(extent={{64,0},{84,20}}))); -5: Documentation too short, Name 'sink' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sink. Affected line: Modelica.Fluid.Sources.Boundary_pT sink(nPorts=1, redeclare package Medium = Medium) "Sink" annotation (Placement(transformation(extent={{68,-10},{48,10}}))); +9: Missing documentation, Name 'prescribedHeatFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: prescribed, Heat. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow prescribedHeatFlow annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=270, origin={64,40}))); -6: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Controls.Continuous.LimPID conPID(u_m(unit="K"), controllerType=Modelica.Blocks.Types.SimpleController.PI, k=1, Ti=5, Td=1, yMax=1, yMin=0) annotation (Placement(transformation(extent={{-44,58},{-24,78}}))); +10: Missing documentation, Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( amplitude=-9000, f=4/86400, offset=-45000) annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=0, origin={50,68}))); -7: Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( amplitude=5, f=100/(3600*24), phase=0, offset=273.15 + 75, startTime=700) "Ambient air temperature" annotation (Placement(transformation(extent={{-100,58},{-80,78}}))); +11: Missing documentation, Name 'sine1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine1( amplitude=5, f=4/86400, offset=278.15) annotation (Placement(transformation(extent={{-128,46},{-108,66}}))); +12: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sensors.TemperatureTwoPort senTRet( redeclare final package Medium = AixLib.Media.Water, final m_flow_nominal=modularBoiler.m_flow_nominal, final initType=Modelica.Blocks.Types.Init.InitialState, final transferHeat=false, final m_flow_small=0.001) "Temperature sensor of cold side of heat generator (supply)" annotation ( Placement(transformation( extent={{10,-10},{-10,10}}, rotation=0, origin={24,-62}))); -AixLib/Fluid/BoilerCHP/BoilerGeneric.mo -1: Name 'internalCapacity' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: internal, Capacity. Affected line: Modelica.Thermal.HeatTransfer.Components.HeatCapacitor internalCapacity(final C=C, T(start=T_start)) "Boiler thermal capacity (dry weight)" annotation (Placement(transformation( extent={{-10,10},{10,-10}}, rotation=90, origin={-18,-50}))); -2: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: BaseClasses.OffDesignOperation offDesignOperation( QNom=QNom, TSupNom=TSupNom, TRetNom=TRetNom) "off design operation" annotation (Placement(transformation(extent={{30,70},{50,90}}))); +AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/FeedbackControl.mo +1: Missing documentation, Name 'PIValve' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Valve. Affected line: public Modelica.Blocks.Continuous.LimPID PIValve( final controllerType=Modelica.Blocks.Types.SimpleController.PI, final k=k, final Ti=Ti, final yMax=yMax, final yMin=yMin, initType=Modelica.Blocks.Types.Init.InitialOutput, y_start=yMin) annotation (Placement(transformation( extent={{10,10},{-10,-10}}, rotation=180, origin={-2,0}))); -3: Name 'conductanceToEnv' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: conductance. Affected line: Modelica.Thermal.HeatTransfer.Components.ThermalConductor conductanceToEnv(final G= 0.0465*QNom/1000 + 4.9891) "Thermal resistance of the boiler casing" annotation (Placement(transformation( extent={{6,-6},{-6,6}}, rotation=180, origin={-38,-34}))); +2: Name 'yValve' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Valve. Affected line: Modelica.Blocks.Interfaces.RealOutput yValve "Position of feedback valve" annotation (Placement(transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={110,0}))); -4: Name 'fixedTemperature' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fixed, Temperature. Affected line: Modelica.Thermal.HeatTransfer.Sources.FixedTemperature fixedTemperature(T( displayUnit="K") = 293.15) "Temperature of environment around the boiler to account for heat losses" annotation (Placement(transformation(extent={{14,-40},{2,-28}}))); +3: Name 'TReturnMea' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Return. Affected line: Modelica.Blocks.Interfaces.RealInput TReturnMea(unit="K") "Measured return temperature" annotation (Placement(transformation(extent={{-122,-20},{-82,20}}))); -5: Missing documentation, Name 'heatFlowSensor' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heat, Sensor. Affected line: Modelica.Thermal.HeatTransfer.Sensors.HeatFlowSensor heatFlowSensor annotation (Placement(transformation(extent={{-26,-28},{-14,-40}}))); +4: Missing documentation. Affected line: Modelica.Blocks.Math.Gain gain1(final k=-1) annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=0, origin={-34,0}))); -6: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,90},{10,110}}))); +5: Missing documentation. Affected line: Modelica.Blocks.Math.Gain gain2(final k=-1) annotation (Placement(transformation( extent={{-6,-6},{6,6}}, rotation=0, origin={-68,-34}))); -7: Documentation too short, Name 'temperatureSensor' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: temperature, Sensor. Affected line: Modelica.Thermal.HeatTransfer.Sensors.TemperatureSensor temperatureSensor( final T(unit="K")) annotation (Placement(transformation(extent={{-50,-26},{-30,-6}}))); +6: Name 'k' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Real k=1 "Gain of controller" annotation (Dialog(group="Feedback Return Control")); -8: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: BaseClasses.DesignOperation designOperation( QNom=QNom, TSupNom=TSupNom, TRetNom=TRetNom) "designOperation for design fuel power" annotation (Placement(transformation(extent={{-60,70},{-40,90}}))); +7: Name 'Ti' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ti. Affected line: parameter Modelica.Units.SI.Time Ti=0.5 "Time constant of Integrator block" annotation (Dialog(group="Feedback Return Control")); -9: Name 'fuelPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fuel, Power. Affected line: Modelica.Blocks.Math.Product fuelPower(final y(unit="W")) "fuel power" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=-90, origin={-44,48}))); -10: Name 'thermalPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: thermal, Power. Affected line: Modelica.Blocks.Math.Product thermalPower(final y(unit="W")) "thermal power" annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=-90, origin={-38,14}))); +AixLib/Systems/ModularEnergySystems/ModularBoiler/Examples/ModularBoilerSimple.mo +1: Name 'k' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Integer k=2 "number of consumers"; -11: Name 'coeffPresLoss' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: coeff, Pres, Loss. Affected line: protected parameter Real coeffPresLoss=7.143*10^8*exp(-0.007078*QNom/1000) "Pressure loss coefficient of the heat generator"; +2: Missing documentation, Name 'MediumWater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Medium, Water. Affected line: package MediumWater = AixLib.Media.Water; +3: Documentation too short, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: ModularBoiler modularBoiler( hasPump=true, QNom=50000, T_start=303.15, hasFeedback=false, use_tableData=true, redeclare function HeatingCurveFunction = AixLib.Controls.SetPoints.Functions.HeatingCurveFunction, dp_Valve(displayUnit="Pa") = 6000, use_HeaCur=false, Kv=10, energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial, redeclare package Medium = MediumWater) annotation (Placement(transformation(extent={{-34,-30},{26,30}}))); -AixLib/Fluid/BoilerCHP/Boiler.mo -1: Name 'paramBoiler' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: param, Boiler. Affected line: parameter AixLib.DataBase.Boiler.General.BoilerTwoPointBaseDataDefinition paramBoiler "Parameters for Boiler" annotation (Dialog(tab = "General", group = "Boiler type"), choicesAllMatching = true); +4: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.Sources.Boundary_pT bou( use_T_in=false, redeclare package Medium = MediumWater, T=293.15, nPorts=1) annotation (Placement(transformation(extent={{-96,-12},{-72,12}}))); -2: Name 'paramHC' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: param. Affected line: parameter AixLib.DataBase.Boiler.DayNightMode.HeatingCurvesDayNightBaseDataDefinition paramHC "Parameters for heating curve" annotation (Dialog(group="Heating curves"), choicesAllMatching=true); +5: Missing documentation, Name 'boilerControlBus' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boiler, Control. Affected line: AixLib.Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,52},{10,72}}))); -3: Name 'KR' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: K. Affected line: parameter Real KR=1 "Gain of Boiler heater" annotation (Dialog(tab = "General", group = "Boiler type")); +6: Missing documentation. Affected line: Modelica.Blocks.Sources.Constant TFlowSet(k=273 + 60) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-86,40}))); -4: Name 'TN' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: N. Affected line: parameter Modelica.Units.SI.Time TN=0.1 "Time Constant of boiler heater (T>0 required)" annotation (Dialog(tab="General", group="Boiler type")); +7: Missing documentation. Affected line: Modelica.Blocks.Sources.BooleanConstant isOnSet(k=true) annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-88,76}))); -5: Name 'riseTime' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: rise. Affected line: parameter Modelica.Units.SI.Time riseTime=30 "Rise/Fall time for step input(T>0 required)" annotation (Dialog(tab="General", group="Boiler type")); +8: Missing documentation, Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Fluid.MixingVolumes.MixingVolume vol( redeclare package Medium = AixLib.Media.Water, T_start=323.15, m_flow_nominal=modularBoiler.m_flow_nominal, V=0.1, nPorts=2) annotation (Placement(transformation(extent={{64,0},{84,20}}))); -6: Name 'declination' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: declination. Affected line: parameter Real declination=1.1 "Declination" annotation(Dialog(tab="External Control")); +9: Missing documentation, Name 'prescribedHeatFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: prescribed, Heat. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow prescribedHeatFlow annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=270, origin={64,40}))); -7: Name 'Tdelta_Max' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Tdelta_. Affected line: parameter Modelica.Units.SI.TemperatureDifference Tdelta_Max=2 "Difference from set flow temperature over which boiler stops" annotation (Dialog(tab="External Control")); +10: Missing documentation, Name 'sine' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine( amplitude=-5000, f=4/86400, offset=-25000) annotation (Placement(transformation(extent={{-10,-10},{10,10}}, rotation=0, origin={50,68}))); -8: Name 'Tdelta_Min' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Tdelta_. Affected line: parameter Modelica.Units.SI.TemperatureDifference Tdelta_Min=2 "Difference from set flow temperature under which boiler starts" annotation (Dialog(tab="External Control")); +11: Missing documentation, Name 'sine1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: sine. Affected line: Modelica.Blocks.Sources.Sine sine1( amplitude=5, f=4/86400, offset=278.15) annotation (Placement(transformation(extent={{-128,46},{-108,66}}))); -9: Name 'Fb' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Fb. Affected line: parameter Modelica.Units.SI.Time Fb=3600 "Period of time for increased set temperature" annotation (Dialog(tab="External Control")); -10: Name 'FA' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: F. Affected line: parameter Real FA=0.2 "Increment for increased set temperature" annotation(Dialog(tab="External Control")); +AixLib/Fluid/BoilerCHP/BoilerNoControl.mo +1: Name 'paramBoiler' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: param, Boiler. Affected line: parameter AixLib.DataBase.Boiler.General.BoilerTwoPointBaseDataDefinition paramBoiler "Parameters for Boiler" annotation (Dialog(tab="General", group= "Boiler type"), choicesAllMatching=true); -11: Name 'TAmbient' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ambient. Affected line: Modelica.Blocks.Interfaces.RealInput TAmbient( final quantity="ThermodynamicTemperature", final unit="K", displayUnit="degC") "Ambient air temperature" annotation (Placement( transformation(extent={{-100,40},{-60,80}}), iconTransformation(extent= {{-80,60},{-60,80}}))); +2: Name 'G' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance G=0.003*Q_nom/50 "Constant thermal conductance to environment(G=Q_loss/dT)"; -12: Name 'switchToNightMode' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: switch, Night, Mode. Affected line: Modelica.Blocks.Interfaces.BooleanInput switchToNightMode "Connector of Boolean input signal" annotation (Placement(transformation( extent={{-100,10},{-60,50}}), iconTransformation(extent={{-80,30},{-60, 50}}))); +3: Name 'Q_nom' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Q_nom. Affected line: parameter Modelica.Units.SI.Power Q_nom=paramBoiler.Q_nom "Nominal heating power"; -13: Name 'ExtControl' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Control. Affected line: replaceable model ExtControl = AixLib.Fluid.BoilerCHP.BaseClasses.Controllers.ExternalControlNightDayHC constrainedby AixLib.Fluid.BoilerCHP.BaseClasses.Controllers.PartialExternalControl "External control" annotation (Dialog(tab="External Control"),choicesAllMatching=true); +4: Name 'internalCapacity' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: internal, Capacity. Affected line: Modelica.Thermal.HeatTransfer.Components.HeatCapacitor internalCapacity( final C=C, T(start=T_start)) "Boiler thermal capacity (dry weight)" annotation (Placement(transformation( extent={{-10,10},{10,-10}}, rotation=90, origin={2,-40}))); +5: Name 'ConductanceToEnv' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Conductance. Affected line: Modelica.Thermal.HeatTransfer.Components.ThermalConductor ConductanceToEnv( final G=G) "Thermal resistance of the boiler casing" annotation ( Placement(transformation( extent={{10,-10},{-10,10}}, rotation=180, origin={-30,-20}))); -AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/FirRatMinCheck.mo -1: Missing documentation, Name 'greaterEqualThreshold' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: greater, Equal, Threshold. Affected line: Modelica.Blocks.Logical.GreaterEqualThreshold greaterEqualThreshold(final threshold=FirRatMin) annotation (Placement(transformation(extent={{-66,-8},{-50,8}}))); +6: Name 'QgasCalculation' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Qgas, Calculation. Affected line: Modelica.Blocks.Math.Product QgasCalculation "Calculate gas usage" annotation (Placement(transformation(extent={{-20,80},{0,100}}))); -2: Missing documentation. Affected line: Modelica.Blocks.Interfaces.RealOutput FirRat annotation (Placement( transformation(extent={{100,-10},{120,10}}))); +7: Name 'limiter' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: limiter. Affected line: Modelica.Blocks.Nonlinear.Limiter limiter(final uMax=1, final uMin=0) "Limits the rel power between 0 and 1" annotation (Placement(transformation(extent={{-80,60},{-60,80}}))); -3: Missing documentation, Name 'realExpression1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Expression. Affected line: Modelica.Blocks.Sources.RealExpression realExpression1(y=FirRatMin) annotation (Placement(transformation(extent={{2,12},{22,32}}))); +8: Name 'NominalGasConsumption' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Nominal, Consumption. Affected line: Modelica.Blocks.Sources.RealExpression NominalGasConsumption(final y=Q_nom/ max(etaLoadBased[:,2]*max(etaTempBased[:,2]))) "Nominal gas power" annotation (Placement(transformation(extent={{-62,88},{-34,104}}))); -4: Missing documentation, Name 'switch4' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: switch4. Affected line: Modelica.Blocks.Logical.Switch switch4 annotation (Placement(transformation(extent={{40,26},{60,46}}))); +9: Name 'fuelPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fuel, Power. Affected line: Modelica.Blocks.Interfaces.RealOutput fuelPower "Connector of Real output signal" annotation (Placement(transformation( extent={{100,90},{120,110}}), iconTransformation(extent={{-10,-10},{10, 10}}, rotation=0, origin={72,110}))); -5: Missing documentation. Affected line: Modelica.Blocks.Logical.And and1 annotation (Placement(transformation(extent={{-30,-2},{-10,18}}))); +10: Name 'thermalPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: thermal, Power. Affected line: Modelica.Blocks.Interfaces.RealOutput thermalPower "Value of Real output" annotation (Placement(transformation(extent={{100,70},{120,90}}), iconTransformation(extent={{62,74},{82,94}}))); +11: Name 'u_rel' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: u_rel. Affected line: Modelica.Blocks.Interfaces.RealInput u_rel "Relative gas power [0,1]" annotation (Placement(transformation( extent={{-20,-20},{20,20}}, rotation=270, origin={-80,120}), iconTransformation( extent={{-10,-10},{10,10}}, rotation=0, origin={-70,70}))); -AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/BoilerControl.mo -1: Name 'TReturnNom' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Return. Affected line: parameter Modelica.Units.SI.Temperature TReturnNom=323.15 "Nominal return temperature" annotation (Dialog(group="Nominal Condition")); +12: Name 'T_amb' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb. Affected line: Modelica.Thermal.HeatTransfer.Interfaces.HeatPort_b T_amb "Heat port for heat losses to ambient" annotation ( Placement(transformation(extent={{30,-30},{50,-10}}), iconTransformation( extent={{58,-60},{78,-40}}))); -2: Name 'kFloTem' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k. Affected line: parameter Real kFloTem=1 "Gain of controller" annotation (Dialog(group= "Flow Temperature Control")); +13: Name 'efficiencyTableLoadDepending' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: efficiency, Table, Load, Depending. Affected line: Modelica.Blocks.Tables.CombiTable1Dv efficiencyTableLoadDepending( final tableOnFile=false, final table=etaLoadBased, final columns={2}, final smoothness=Modelica.Blocks.Types.Smoothness.ContinuousDerivative) "Table with efficiency parameters" annotation (Placement(transformation(extent={{-40,50},{-19,71}}))); -3: Name 'TiFloTem' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ti. Affected line: parameter Modelica.Units.SI.Time TiFloTem=10 "Time constant of Integrator block" annotation (Dialog(group= "Flow Temperature Control")); +14: Name 'QflowCalculation' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Qflow, Calculation. Affected line: Modelica.Blocks.Math.Product QflowCalculation "Calculation of the produced heatflow" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=270, origin={-60,2}))); -4: Name 'use_tableData' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: use_table, Data. Affected line: parameter Boolean use_tableData=true "Choose between tables or function to calculate TSet" annotation (Dialog(group="Heating Curve")); +15: Name 'etaLoadBased' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Load, Based. Affected line: parameter Real etaLoadBased[:,2]=paramBoiler.eta "Table matrix for part load based efficiency (e.g. [0,0.99; 0.5, 0.98; 1, 0,97])"; -5: Missing documentation, Name 'HeatingCurveFunction' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Heating, Curve, Function. Affected line: replaceable function HeatingCurveFunction = AixLib.Controls.SetPoints.Functions.HeatingCurveFunction annotation ( choicesAllMatching=true, Dialog(group="Heating Curve")); +16: Name 'etaTempBased' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Temp, Based. Affected line: parameter Real etaTempBased[:,2]=[293.15,1.09; 303.15,1.08; 313.15,1.05; 323.15,1.; 373.15,0.99] "Table matrix for temperature based efficiency"; -6: Missing documentation, Name 'declination' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: declination. Affected line: parameter Real declination=1 annotation (Dialog(group="Heating Curve")); +17: Name 'etaCalculation' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Calculation. Affected line: Modelica.Blocks.Math.Product etaCalculation "calculates the efficiency of the boiler" annotation (Placement( transformation( extent={{-10,-10},{10,10}}, rotation=0, origin={10,50}))); -7: Missing documentation, Name 'day_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: day_hour. Affected line: parameter Real day_hour=6 annotation (Dialog(group="Heating Curve")); +18: Name 'efficiencyTableLoadDepending1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: efficiency, Table, Load, Depending. Affected line: Modelica.Blocks.Tables.CombiTable1Dv efficiencyTableLoadDepending1( final tableOnFile=false, final table=etaTempBased, final columns={2}, final smoothness=Modelica.Blocks.Types.Smoothness.ContinuousDerivative) "Table with efficiency parameters" annotation (Placement(transformation(extent={{-40,20},{-19,41}}))); -8: Missing documentation, Name 'night_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: night_hour. Affected line: parameter Real night_hour=22 annotation (Dialog(group="Heating Curve")); -9: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: parameter Utilities.Time.Types.ZeroTime zerTim=AixLib.Utilities.Time.Types.ZeroTime.NY2017 "Enumeration for choosing how reference time (time = 0) should be defined. Used for heating curve" annotation (Dialog(group="Heating Curve")); +AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/heatingCurve.mo +1: Name 'use_tableData' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: use_table, Data. Affected line: parameter Boolean use_tableData=true "Choose between tables or function to calculate TSet" annotation (Dialog(group="Heating Curve")); -10: Name 'TOffset' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Offset. Affected line: parameter Modelica.Units.SI.ThermodynamicTemperature TOffset=0 "Offset to heating curve temperature" annotation (Dialog(group="Heating Curve")); +2: Missing documentation, Name 'declination' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: declination. Affected line: parameter Real declination=1 annotation (Dialog(group="Heating Curve")); -11: Name 'kFeedBack' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: k, Feed, Back. Affected line: parameter Real kFeedBack=1 "Gain of controller" annotation (Dialog(group="Feedback Return Control")); +3: Missing documentation, Name 'day_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: day_hour. Affected line: parameter Real day_hour=6 annotation (Dialog(group="Heating Curve")); -12: Name 'TiFeedBack' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ti, Feed, Back. Affected line: parameter Modelica.Units.SI.Time TiFeedBack=0.5 "Time constant of Integrator block" annotation (Dialog(group= "Feedback Return Control")); +4: Missing documentation, Name 'night_hour' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: night_hour. Affected line: parameter Real night_hour=22 annotation (Dialog(group="Heating Curve")); -13: Name 'yMaxFeedBack' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Feed, Back. Affected line: parameter Real yMaxFeedBack=0.99 "Upper limit of output" annotation (Dialog(group="Feedback Return Control")); +5: Name 'TOffset' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Offset. Affected line: parameter Modelica.Units.SI.ThermodynamicTemperature TOffset=0 "Offset to heating curve temperature" annotation (Dialog(group="Heating Curve")); -14: Name 'yMinFeedBack' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Feed, Back. Affected line: parameter Real yMinFeedBack=0 "Lower limit of output" annotation (Dialog(group="Feedback Return Control")); +6: Missing documentation, Name 'heatingCurve' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heating, Curve. Affected line: AixLib.Controls.SetPoints.HeatingCurve heatingCurve( final TOffset=TOffset, final use_dynTRoom=false, final zerTim=zerTim, final day_hour=day_hour, final night_hour=night_hour, final heatingCurveRecord= AixLib.DataBase.Boiler.DayNightMode.HeatingCurves_Vitotronic_Day23_Night10(), final declination=declination, redeclare function HeatingCurveFunction = HeatingCurveFunction, final use_tableData=use_tableData, final TRoom_nominal=293.15) annotation (Placement(transformation(extent={{-10,-10},{10,10}}))); -15: Missing documentation, Name 'boilerControlBus' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boiler, Control. Affected line: AixLib.Controls.Interfaces.BoilerControlBus boilerControlBus annotation (Placement(transformation(extent={{-10,90},{10,110}}))); +AixLib/Fluid/BoilerCHP/CHPNoControl.mo +1: Name 'param' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: param. Affected line: parameter AixLib.DataBase.CHP.CHPDataSimple.CHPBaseDataDefinition param "CHP data set" annotation (choicesAllMatching=true, Dialog(group="Unit properties")); -AixLib/Fluid/BoilerCHP/BaseClasses/DesignOperation.mo -1: Name 'ReturnTemp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Return, Temp. Affected line: Modelica.Blocks.Sources.RealExpression ReturnTemp(y=TRetNom) "Nominal return temperature" annotation (Placement(transformation(extent={{-100,6},{-54,30}}))); +2: Name 'minCapacity' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Capacity. Affected line: parameter Real minCapacity = 0 "Minimum allowable working capacity (unit [-])" annotation(Dialog(group="Unit properties")); -2: Name 'y_fullLoad' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: y_full, Load. Affected line: Modelica.Blocks.Sources.RealExpression y_fullLoad(y=1) "realtive power" annotation (Placement(transformation(extent={{-100,-52},{-54,-28}}))); +3: Name 'G' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: G. Affected line: parameter Modelica.Units.SI.ThermalConductance G=0.003*param.data_CHP[end, 3] /50 "Constant thermal conductance to environment(G=Q_loss/dT)"; -3: Name 'conductance' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: conductance. Affected line: Modelica.Blocks.Sources.RealExpression conductance(y=0.0465*QNom/1000 + 4.9891) "Thermal conductance" annotation (Placement(transformation(extent={{-98,54},{-52,78}}))); +4: Name 'u_rel' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: u_rel. Affected line: Modelica.Blocks.Interfaces.RealInput u_rel( final unit="1") "Relative" annotation (Placement( transformation(extent={{-126,66},{-100,94}}, rotation=0), iconTransformation(extent={{-80,-70},{-60,-50}}))); -4: Missing documentation, Name 'division' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: division. Affected line: Modelica.Blocks.Math.Division division annotation (Placement(transformation(extent={{58,48},{78,68}}))); +5: Name 'electricalPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: electrical, Power. Affected line: Modelica.Blocks.Interfaces.RealOutput electricalPower( final quantity="Power", final unit="W") "Electrical power" annotation (Placement( transformation( origin={20,110}, extent={{-10,-10},{10,10}}, rotation=90), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={-50,90}))); -5: Missing documentation, Name 'multiplex4' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: multiplex4. Affected line: Modelica.Blocks.Routing.Multiplex4 multiplex4 annotation (Placement(transformation(extent={{18,-16},{38,4}}))); +6: Name 'thermalPower' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: thermal, Power. Affected line: Modelica.Blocks.Interfaces.RealOutput thermalPower(final unit="W") "Thermal power" annotation (Placement( transformation( origin={36,110}, extent={{-10,-10},{10,10}}, rotation=90), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={-20,90}))); -6: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: SDF.NDTable boilerEffciency( nin=4, readFromFile=true, filename=ModelicaServices.ExternalReferences.loadResource( "modelica://AixLib/Resources/Data/Fluid/BoilerCHP/BaseClasses/GenericBoiler/Boiler_Generic_Characteristic_Chart.sdf"), dataset="/Characteristic chart", dataUnit="-", scaleUnits={"K","K","-","-"}, interpMethod=SDF.Types.InterpolationMethod.Linear, extrapMethod=SDF.Types.ExtrapolationMethod.Hold) "Characteristic chart of adiabatic boiler efficiency" annotation (Placement(transformation(extent={{54,-16},{74,4}}))); +7: Name 'fuelInput' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fuel, Input. Affected line: Modelica.Blocks.Interfaces.RealOutput fuelInput(final unit="W") "Fuel input" annotation (Placement(transformation( origin={51,110}, extent={{-10,-11},{10,11}}, rotation=90), iconTransformation( extent={{-10,-11},{10,11}}, rotation=90, origin={20,90}))); -7: Missing documentation. Affected line: Modelica.Blocks.Math.Add add annotation (Placement(transformation(extent={{20,54},{40,74}}))); +8: Name 'fuelConsumption' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: fuel, Consumption. Affected line: Modelica.Blocks.Interfaces.RealOutput fuelConsumption "Fuel consumption" annotation (Placement(transformation( origin={66,110}, extent={{-10,-10},{10,10}}, rotation=90), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={50,90}))); -8: Missing documentation. Affected line: Modelica.Blocks.Math.Add add1(k1=-1) annotation (Placement(transformation(extent={{-36,-14},{-16,6}}))); +9: Name 'combiTable1Ds' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: combi, Table, Ds. Affected line: Modelica.Blocks.Tables.CombiTable1Ds combiTable1Ds( tableName="NoName", fileName="NoName", final table=param.data_CHP) "Time table to read CHP performance data" annotation (Placement(transformation(extent={{40,40},{60,60}}, rotation=0))); -9: Name 'SupplyTemp' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Supply, Temp. Affected line: Modelica.Blocks.Sources.RealExpression SupplyTemp(y=TSupNom) "Nominal supply temperature" annotation (Placement(transformation(extent={{-100,-22},{-54,2}}))); +10: Name 'limiter' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: limiter. Affected line: Modelica.Blocks.Nonlinear.Limiter limiter(final uMax=1, final uMin= minCapacity) "Limits the rel power between 0 and 1" annotation (Placement(transformation(extent={{-60,40},{-40,60}}))); -10: Name 'DeltaT_amb' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Delta, T_amb. Affected line: Modelica.Blocks.Sources.RealExpression DeltaT_amb(y=TSupNom - 293.15) "temperature difference supply-ambient" annotation (Placement(transformation(extent={{-100,80},{-54,104}}))); +11: Name 'gain4' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: gain4. Affected line: Modelica.Blocks.Math.Gain gain4(final k=1000) "Conversion factor" annotation (Placement(transformation(extent={{4,-4},{-4,4}}, rotation=270, origin={66,90}))); -11: Name 'losses' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: losses. Affected line: Modelica.Blocks.Math.Product losses "Nominal boiler losses" annotation (Placement(transformation(extent={{-32,76},{-12,96}}))); +12: Name 'gain3' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: gain3. Affected line: Modelica.Blocks.Math.Gain gain3(final k=1000) "Conversion factor" annotation (Placement(transformation(extent={{4,-4},{-4,4}}, rotation=270, origin={50,90}))); + +13: Name 'toPercent' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Percent. Affected line: Modelica.Blocks.Math.Gain toPercent(final k=100) "Conversion factor" annotation (Placement(transformation( extent={{6,-6},{-6,6}}, rotation=180, origin={12,50}))); + +14: Name 'internalCapacity' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: internal, Capacity. Affected line: Modelica.Thermal.HeatTransfer.Components.HeatCapacitor internalCapacity(final C=C, T(start=T_start)) "Boiler thermal capacity (dry weight)" annotation (Placement(transformation( extent={{-10,10},{10,-10}}, rotation=90, origin={2,-40}))); + +15: Name 'ConductanceToEnv' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Conductance. Affected line: Modelica.Thermal.HeatTransfer.Components.ThermalConductor ConductanceToEnv(final G=G) "Thermal resistance of the boiler casing" annotation ( Placement(transformation( extent={{10,-10},{-10,10}}, rotation=180, origin={-30,-20}))); + +16: Name 'T_amb' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: T_amb. Affected line: Modelica.Thermal.HeatTransfer.Interfaces.HeatPort_b T_amb "Heat port for heat losses to ambient" annotation ( Placement(transformation(extent={{30,-30},{50,-10}}), iconTransformation( extent={{58,-60},{78,-40}}))); + + +AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/SafetyControl.mo +1: Missing documentation. Affected line: Modelica.Blocks.Sources.RealExpression TFlowMaxExp(final y=TFlowMax) annotation (Placement(transformation(extent={{-96,-30},{-76,-10}}))); + +2: Missing documentation, Name 'greater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: greater. Affected line: Modelica.Blocks.Logical.Greater greater annotation (Placement(transformation(extent={{-48,-10},{-28,10}}))); AixLib/Fluid/BoilerCHP/CHP.mo @@ -592,4 +476,48 @@ AixLib/Fluid/BoilerCHP/CHP.mo 22: Name 'booleanConstant' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: boolean, Constant. Affected line: Modelica.Blocks.Sources.BooleanConstant booleanConstant(k=ctrlStrategy) "Determines control strategy" annotation (Placement(transformation(extent={{-26,-54},{-14,-42}}, rotation=0))); -23: Name 'exothermicTemperature' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: exothermic, Temperature. Affected line: Modelica.Blocks.Sources.Constant exothermicTemperature(k=1783.4) "Exothermic temperature" annotation (Placement(transformation(extent={{52,12},{68,28}}))); \ No newline at end of file +23: Name 'exothermicTemperature' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: exothermic, Temperature. Affected line: Modelica.Blocks.Sources.Constant exothermicTemperature(k=1783.4) "Exothermic temperature" annotation (Placement(transformation(extent={{52,12},{68,28}}))); + + +AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/FirRatMinCheck.mo +1: Missing documentation, Name 'greaterEqualThreshold' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: greater, Equal, Threshold. Affected line: Modelica.Blocks.Logical.GreaterEqualThreshold greaterEqualThreshold(final threshold=FirRatMin) annotation (Placement(transformation(extent={{-66,-8},{-50,8}}))); + +2: Missing documentation. Affected line: Modelica.Blocks.Interfaces.RealOutput FirRat annotation (Placement( transformation(extent={{100,-10},{120,10}}))); + +3: Missing documentation, Name 'realExpression1' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: real, Expression. Affected line: Modelica.Blocks.Sources.RealExpression realExpression1(y=FirRatMin) annotation (Placement(transformation(extent={{2,12},{22,32}}))); + +4: Missing documentation, Name 'switch4' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: switch4. Affected line: Modelica.Blocks.Logical.Switch switch4 annotation (Placement(transformation(extent={{40,26},{60,46}}))); + +5: Missing documentation. Affected line: Modelica.Blocks.Logical.And and1 annotation (Placement(transformation(extent={{-30,-2},{-10,18}}))); + + +AixLib/Systems/ModularEnergySystems/ModularBoiler/Controls/InternalFirRatControl.mo +1: Name 'Ti' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Ti. Affected line: parameter Modelica.Units.SI.Time Ti=10 "Time constant of Integrator block" annotation (Dialog(group="Flow Temperature PI")); + +2: Documentation too short. Affected line: Modelica.Blocks.Interfaces.RealInput TFlowMea(unit="K") annotation (Placement( transformation( extent={{-20,-20},{20,20}}, rotation=0, origin={-120,-52}))); + +3: Missing documentation. Affected line: Modelica.Blocks.Interfaces.RealOutput FirRatSet annotation (Placement(transformation(extent={{100,-10},{120,10}}))); + + +AixLib/Fluid/BoilerCHP/BaseClasses/PartialHeatGenerator.mo +1: Name 'transferHeat' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: transfer, Heat. Affected line: parameter Boolean transferHeat=false "If true, temperature T converges towards TAmb when no flow" annotation (Dialog(tab="Advanced", group="Sensor Properties")); + +2: Name 'm_flow_start' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: m_flow. Affected line: parameter Modelica.Units.SI.MassFlowRate m_flow_start=0 "Guess value of m_flow = port_a.m_flow" annotation (Dialog(tab="Initialization")); + +3: Name 'a' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: a. Affected line: parameter Real a "Coefficient of old approach from model Modelica.Fluid.Fittings.GenericResistances.VolumeFlowRate. Recalculated to dp_nominal based on IBPSA approach." annotation (Dialog(tab="Advanced", group="Pressure drop")); + +4: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: Sensors.TemperatureTwoPort senTRet( redeclare final package Medium = Medium, final tau=tau, final m_flow_nominal=m_flow_nominal, final initType=initType, final T_start=T_start, final transferHeat=transferHeat, final TAmb=TAmb, final tauHeaTra=tauHeaTra, final allowFlowReversal=allowFlowReversal, final m_flow_small=m_flow_small) "Temperature sensor of cold side of heat generator (return)" annotation (Placement(transformation(extent={{-80,-90},{-60,-70}})));Sensors.TemperatureTwoPort senTSup( redeclare final package Medium = Medium, final tau=tau, final m_flow_nominal=m_flow_nominal, final initType=initType, final T_start=T_start, final transferHeat=transferHeat, final TAmb=TAmb, final tauHeaTra=tauHeaTra, final allowFlowReversal=allowFlowReversal, final m_flow_small=m_flow_small) "Temperature sensor of hot side of heat generator (supply)" annotation (Placement(transformation(extent={{30,-90},{50,-70}})));Sensors.MassFlowRate senMasFlo( redeclare final package Medium = Medium, final allowFlowReversal=allowFlowReversal) "Sensor for mass flwo rate" annotation (Placement(transformation(extent={{60,-90},{80,-70}}))); + +5: Name 'heater' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: heater. Affected line: Modelica.Thermal.HeatTransfer.Sources.PrescribedHeatFlow heater "Prescribed heat flow" annotation ( Placement(transformation( extent={{-10,-10},{10,10}}, rotation=-90, origin={-60,-50}))); + +6: Could not extract name from line and check correctness, is your type specification correct (full library path)?. Affected line: MixingVolumes.MixingVolume vol( redeclare final package Medium = Medium, final m_flow_nominal=m_flow_nominal, final m_flow_small=m_flow_small, final allowFlowReversal=allowFlowReversal, final nPorts=2, final p_start=p_start, final T_start=T_start) "Fluid volume" annotation (Placement(transformation(extent={{-50,-80},{-30,-60}})));FixedResistances.PressureDrop preDro( redeclare final package Medium = Medium, final m_flow_nominal=m_flow_nominal, final show_T=false, final allowFlowReversal=allowFlowReversal, final dp_nominal=dp_nominal) "Pressure drop" annotation (Placement(transformation(extent={{-20,-90},{0,-70}}))); + +7: Name 'rho_default' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: rho_default. Affected line: final parameter Modelica.Units.SI.Density rho_default=Medium.density_pTX( Medium.p_default, Medium.T_default, Medium.X_default) "Density used for parameterization of pressure curve" annotation (Dialog(tab="Advanced", group="Pressure drop")); + + +AixLib/Fluid/BoilerCHP/HeatGeneratorNoControl.mo +1: Name 'TCold' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: Cold. Affected line: Modelica.Blocks.Interfaces.RealOutput TCold( final quantity="ThermodynamicTemperature", final unit="K", displayUnit="degC") "Temperature of the passing fluid" annotation (Placement(transformation(extent={{44,76},{64,96}}), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={-40,90}))); + +2: Name 'massFlow' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: mass. Affected line: Modelica.Blocks.Interfaces.RealOutput massFlow(quantity="MassFlowRate", final unit="kg/s") "Mass flow rate from port_a to port_b" annotation (Placement(transformation(extent={{100,30},{120,50}}), iconTransformation( extent={{-10,-10},{10,10}}, rotation=90, origin={40,90}))); + +3: Name 'coeffPresLoss' contains parts with more/less than 3 characters or which are not part of special cases. Affected parts: coeff, Pres, Loss. Affected line: parameter Real coeffPresLoss "Pressure loss coefficient of the heat generator"; \ No newline at end of file diff --git a/docs/issue1147_GenericBoiler/regression/Fluid/comparison-dymola.log b/docs/issue1147_GenericBoiler/regression/Fluid/comparison-dymola.log new file mode 100644 index 0000000000..bc8033ce1e --- /dev/null +++ b/docs/issue1147_GenericBoiler/regression/Fluid/comparison-dymola.log @@ -0,0 +1,1622 @@ +[ + { + "comparison": { + "file_name": "AixLib.Fluid.FixedResistances.Examples.SimplePipe.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Fluid.FixedResistances.Examples.SimplePipe.mat_senTemIn.T", + "funnel_comp/AixLib.Fluid.FixedResistances.Examples.SimplePipe.mat_senTemOut.T" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1 + ], + "var_groups": [ + 0, + 0 + ], + "variables": [ + "senTemIn.T", + "senTemOut.T" + ], + "warnings": [ + null, + null + ] + }, + "model": "AixLib.Fluid.FixedResistances.Examples.SimplePipe", + "simulation": { + "elapsed_time": 0.00769, + "final_time": 1000, + "jacobians": 43, + "start_time": 0, + "state_events": 0, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.mat_rampValvePosition.y", + "funnel_comp/AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.mat_pump.pumpBus.dpMea", + "funnel_comp/AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.mat_pump.pumpBus.dpSet", + "funnel_comp/AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.mat_pump.pumpBus.onSet" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 1, + 1, + 2 + ], + "variables": [ + "rampValvePosition.y", + "pump.pumpBus.dpMea", + "pump.pumpBus.dpSet", + "pump.pumpBus.onSet" + ], + "warnings": [ + null, + null, + null, + null + ] + }, + "model": "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled", + "simulation": { + "elapsed_time": 0.00977, + "final_time": 600, + "jacobians": 108, + "start_time": 0, + "state_events": 0, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.mat_dpControlled_dp.mov.dpMachine", + "funnel_comp/AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.mat_dpControlled_dp.mov.m_flow", + "funnel_comp/AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.mat_m_flow_nominal", + "funnel_comp/AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.mat_dpControlled_dp.mov.dpMachine", + "funnel_comp/AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.mat_dp_nominal", + "funnel_comp/AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.mat_val.y_actual", + "funnel_comp/AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.mat_elEnergy" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1, + 1, + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 1, + 1, + 2, + 2, + 3, + 4 + ], + "variables": [ + "dpControlled_dp.mov.dpMachine", + "dpControlled_dp.mov.m_flow", + "m_flow_nominal", + "dpControlled_dp.mov.dpMachine", + "dp_nominal", + "val.y_actual", + "elEnergy" + ], + "warnings": [ + null, + null, + null, + null, + null, + null, + null + ] + }, + "model": "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst", + "simulation": { + "elapsed_time": 0.0312, + "final_time": 3600, + "jacobians": 120, + "start_time": 0, + "state_events": 0, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.mat", + "funnel_dirs": [ + null, + null + ], + "success_rate": 0.0, + "t_err_max": [ + 0, + 0 + ], + "test_passed": [ + 0, + 0 + ], + "var_groups": [ + 0, + 0 + ], + "variables": [ + "TSet.y", + "combinedHeatPower.senTHot.T" + ], + "warnings": [ + "Translation, simulation or extracting simulation results failed. Fluid/BoilerCHP/Examples/CHPSystem.mos uses combinedHeatPower.senTHot.T which does not exist in AixLib.Fluid.BoilerCHP.Examples.CHPSystem.mat.\n", + "" + ] + }, + "model": "AixLib.Fluid.BoilerCHP.Examples.CHPSystem", + "simulation": { + "elapsed_time": 0.028, + "final_time": 1200, + "jacobians": 409, + "start_time": 0, + "state_events": 5, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_supply.T", + "funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.senT_return.T", + "funnel_comp/AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat_demand.port_a.m_flow" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 0, + 1 + ], + 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+167615.999000,344.488388 +169343.999000,344.446469 +171071.999000,344.049039 +172799.999000,344.003004 +172800.001000,344.003004 diff --git a/docs/issue1147_GenericBoiler/regression/Fluid/funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_temperatureSensor.T/reference.csv b/docs/issue1147_GenericBoiler/regression/Fluid/funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_temperatureSensor.T/reference.csv new file mode 100644 index 0000000000..d848b8f5a4 --- /dev/null +++ b/docs/issue1147_GenericBoiler/regression/Fluid/funnel_comp/AixLib.Fluid.Storage.Examples.StorageSolarCollector.mat_temperatureSensor.T/reference.csv @@ -0,0 +1,102 @@ +x,y +0.000000,293.149994 +1728.000000,298.446716 +3456.000000,298.469940 +5184.000000,298.491943 +6912.000000,298.512329 +8640.000000,298.531586 +10368.000000,298.549286 +12096.000000,298.566040 +13824.000000,298.581299 +15552.000000,298.595795 +17280.000000,298.609039 +19008.000000,298.814148 +20736.000000,299.531799 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+3455.999000,298.768410 +5183.999000,298.790435 +6911.999000,298.810841 +8639.999000,298.830117 +10367.999000,298.847835 +12095.999000,298.864606 +13823.999000,298.879880 +15551.999000,298.894390 +17279.999000,298.907648 +19007.999000,299.112962 +20735.999000,299.831331 +22463.999000,301.046595 +24191.999000,302.777664 +25919.999000,304.992218 +27647.999000,307.673669 +29375.999000,310.785053 +31103.999000,314.282077 +32831.999000,318.122675 +34559.999000,322.227759 +36287.999000,326.544083 +38015.999000,330.984768 +39743.999000,335.489818 +41471.999000,339.976508 +43199.999000,344.400086 +44927.999000,347.958023 +44928.001000,347.958023 +46656.001000,346.965179 +48384.001000,344.536239 +50112.001000,343.368660 +51840.000837,342.722354 +53567.999000,342.779601 +55295.999000,343.030401 +57023.999000,343.253555 +57024.001000,343.253555 +58752.001000,343.187816 +60480.001000,342.887467 +62208.001000,342.415713 +63936.001000,341.944966 +65664.001000,341.738156 +67392.001000,341.711671 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+134783.999000,350.789648 +136511.999000,350.891679 +136512.001000,350.891679 +138240.001000,350.561851 +139968.001000,350.214061 +141696.001000,349.499052 +143424.001000,348.760858 +145152.001000,347.900684 +146880.001000,347.412770 +148608.001000,347.013934 +150336.001000,346.802389 +152064.001000,346.640178 +153792.001000,346.512059 +155520.001000,346.438897 +157248.001000,346.279405 +158976.001000,346.221272 +160704.001000,345.983486 +162432.001000,345.923948 +164160.001000,345.605972 +165888.001000,345.555996 +167616.001000,345.178055 +169344.001000,345.136051 +171072.001000,344.737826 +172800.001000,344.691698 diff --git a/docs/issue1147_GenericBoiler/regression/Fluid/simulator-dymola.log b/docs/issue1147_GenericBoiler/regression/Fluid/simulator-dymola.log new file mode 100644 index 0000000000..f1e96d42fe --- /dev/null +++ b/docs/issue1147_GenericBoiler/regression/Fluid/simulator-dymola.log @@ -0,0 +1,3972 @@ + = true + + +rCheck = checkModel("AixLib.Fluid.FixedResistances.Examples.SimplePipe"); +Check of AixLib.Fluid.FixedResistances.Examples.SimplePipe: +The model has the same number of unknowns and equations: 368 +The model could not be deduced to be symbolically well-posed. +The model has + 360+simplePipe.vol[1].dynBal.nPorts+simplePipe.vol[2].dynBal.nPorts+ simplePipe.vol[3].dynBal.nPorts+simplePipe.vol[4].dynBal.nPorts +scalar unknowns and + 334+2*Source.nPorts+(if not Source.use_m_flow_in then 1 else 0)+(if not Source.use_T_in then 1 else 0)+(if not Source.use_X_in then 1 else 0)+2* Sink.nPorts+(if not simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* simplePipe.vol[1].dynBal.nPorts+(if not simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*simplePipe.vol[2].dynBal.nPorts+(if not simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*simplePipe.vol[3].dynBal.nPorts+(if not simplePipe.vol[4].dynBal.use_mWat_flow then 1 else 0)+3*simplePipe.vol[4].dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 368 +Check of AixLib.Fluid.FixedResistances.Examples.SimplePipe successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/SimplePipe.mos\",", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.FixedResistances.Examples.SimplePipe\",", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.FixedResistances.Examples.SimplePipe\\\");\",", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.FixedResistances.Examples.SimplePipe.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/SimplePipe.mos"); +translateModel("AixLib.Fluid.FixedResistances.Examples.SimplePipe"); +Translation of AixLib.Fluid.FixedResistances.Examples.SimplePipe: +The DAE has 368 scalar unknowns and 368 scalar equations. + +Statistics + +Original Model + Number of components: 80 + Variables: 963 + Constants: 18 (18 scalars) + Parameters: 450 (428 scalars) + Unknowns: 495 (378 scalars) + Differentiated variables: 14 scalars + Equations: 363 + Nontrivial: 270 +Translated Model + Constants: 341 scalars + Free parameters: 44 scalars + Parameter depending: 126 scalars + Continuous time states: 10 scalars + Time-varying variables: 71 scalars + Alias variables: 242 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + senTemIn.T + senTemOut.T + simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + simplePipe.PipeWall[4].CylindricLoad1.heatCapacitor.T + simplePipe.vol[1].dynBal.U + simplePipe.vol[2].dynBal.U + simplePipe.vol[3].dynBal.U + simplePipe.vol[4].dynBal.U + + = true +simulateModel("AixLib.Fluid.FixedResistances.Examples.SimplePipe", stopTime=1000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.FixedResistances.Examples.SimplePipe"); +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.FixedResistances.Examples.SimplePipe.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe"); +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe: +The model has the same number of unknowns and equations: 175 +The model could not be deduced to be symbolically well-posed. +The model has + 173+pip.vol.dynBal.nPorts +scalar unknowns and + 159+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if not pip.vol.dynBal.use_mWat_flow then 1 else 0)+3* pip.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 175 +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/StaticPipe.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/StaticPipe.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe: +The DAE has 175 scalar unknowns and 175 scalar equations. + +Statistics + +Original Model + Number of components: 33 + Variables: 506 + Constants: 10 (10 scalars) + Parameters: 251 (244 scalars) + Unknowns: 245 (181 scalars) + Differentiated variables: 4 scalars + Equations: 205 + Nontrivial: 171 +Translated Model + Constants: 185 scalars + Free parameters: 45 scalars + Parameter depending: 61 scalars + Continuous time states: 3 scalars + Time-varying variables: 31 scalars + Alias variables: 113 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + pip.vol.dynBal.U + senTemIn.T + senTemOut.T + + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe", stopTime=1000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe"); +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.StaticPipe.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled"); +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled: +The model has the same number of unknowns and equations: 151 +The model could not be deduced to be symbolically well-posed. +The model has + 140+2*(size(pump.maxMinTable.columns, 1)+pump.deMultiplex3_1.n1+pump.deMultiplex3_1.n2) +pump.criticalDamping.n+pump.vol.dynBal.nPorts +scalar unknowns and + 130+2*size(pump.maxMinTable.columns, 1)+pump.deMultiplex3_1.n1+pump.deMultiplex3_1.n2 +pump.criticalDamping.n+(if vessle.use_Xi_in then 1 else (if vessle.use_X_in then 0 else 1))+(if not vessle.use_p_in then 1 else 0)+2*vessle.nPorts+(if not vessle.use_T_in then 1 else 0)+(if not pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*pump.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 151 +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpHeadControlled.mos\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled\\\");\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpHeadControlled.mos"); +simulateModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled", tolerance=1e-6, stopTime=600, method="dassl", resultFile="AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled"); +Translation of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled: +The DAE has 151 scalar unknowns and 151 scalar equations. + +Statistics + +Original Model + Number of components: 34 + Variables: 378 + Constants: 9 (9 scalars) + Parameters: 177 (481 scalars) + Unknowns: 192 (155 scalars) + Differentiated variables: 5 scalars + Equations: 158 + Nontrivial: 131 +Translated Model + Constants: 136 scalars + Free parameters: 253 scalars + Parameter depending: 127 scalars + Outputs: 7 scalars + Continuous time states: 3 scalars + Time-varying variables: 36 scalars + Alias variables: 93 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + pump.criticalDamping.x[1] + simpleValve.filter.s[1] + simpleValve.filter.s[2] + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpHeadControlled.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger"); +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger: +The model has the same number of unknowns and equations: 5083 +The model could not be deduced to be symbolically well-posed. +The model has + 3373+32*enthalpyExchanger.n+16*enthalpyExchanger.airDuct2.heatTransfer.n+18* enthalpyExchanger.airDuct2.massTransfer.n+16*enthalpyExchanger.airDuct1.heatTransfer.n +18*enthalpyExchanger.airDuct1.massTransfer.n+5*enthalpyExchanger.membrane.heatTransfer.n +enthalpyExchanger.membrane.massTransfer.n+2*enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +scalar unknowns and + 3043+17*enthalpyExchanger.airDuct2.heatTransfer.n+19*enthalpyExchanger.airDuct2.massTransfer.n +3*(if enthalpyExchanger.couFloArr then 2*enthalpyExchanger.n else 0)+17* enthalpyExchanger.airDuct1.heatTransfer.n+19*enthalpyExchanger.airDuct1.massTransfer.n +7*enthalpyExchanger.membrane.heatTransfer.n+3*enthalpyExchanger.membrane.massTransfer.n +2*(if enthalpyExchanger.useConPer then 1 else 0)+32*enthalpyExchanger.n+(if souAirHot.use_Xi_in then 2 else (if souAirHot.use_X_in then 1 else 3))+3* souAirHot.nPorts+(if not souAirHot.use_p_in then 1 else 0)+(if not souAirHot.use_T_in then 1 else 0)+(if sinAirHot.use_Xi_in then 2 else (if sinAirHot.use_X_in then 1 else 3))+3*sinAirHot.nPorts+(if not sinAirHot.use_p_in then 1 else 0)+(if not sinAirHot.use_T_in then 1 else 0)+( if souAirCol.use_Xi_in then 2 else (if souAirCol.use_X_in then 1 else 3))+3* souAirCol.nPorts+(if not souAirCol.use_p_in then 1 else 0)+(if not souAirCol.use_T_in then 1 else 0)+(if sinAirCol.use_Xi_in then 2 else (if sinAirCol.use_X_in then 1 else 3))+3*sinAirCol.nPorts+(if not sinAirCol.use_p_in then 1 else 0)+(if not sinAirCol.use_T_in then 1 else 0)+5 *enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 5083 +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Examples/Test_EnthalpyExchanger.mos\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger\\\");\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Examples/Test_EnthalpyExchanger.mos"); +simulateModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger", stopTime=7200, outputInterval=10, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger"); +Translation of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger: +The DAE has 5083 scalar unknowns and 5083 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + sinAirCol.p(start = 101325) + sinAirHot.p(start = 101325) + +The redundancies involve +initial equations: + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirCol.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + sinAirHot.p = 101325.0; + + +Statistics + +Original Model + Number of components: 556 + Variables: 6181 + Constants: 154 (154 scalars) + Parameters: 2178 (2382 scalars) + Unknowns: 3849 (5219 scalars) + Differentiated variables: 117 scalars + Equations: 2512 + Nontrivial: 1919 +Translated Model + Constants: 2163 scalars + Free parameters: 163 scalars + Parameter depending: 1011 scalars + Continuous time states: 87 scalars + Time-varying variables: 1614 scalars + Alias variables: 2804 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + enthalpyExchanger.airDuct1.senRelHum.phi + enthalpyExchanger.airDuct1.senTem.T + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[1].dynBal.U + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[2].dynBal.U + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[3].dynBal.U + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[4].dynBal.U + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[5].dynBal.U + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[6].dynBal.U + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[7].dynBal.U + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[8].dynBal.U + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[9].dynBal.U + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[10].dynBal.U + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[11].dynBal.U + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[12].dynBal.U + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[13].dynBal.U + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[14].dynBal.U + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[15].dynBal.U + enthalpyExchanger.airDuct2.senRelHum.phi + enthalpyExchanger.airDuct2.senTem.T + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[1].dynBal.U + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[2].dynBal.U + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[3].dynBal.U + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[4].dynBal.U + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[5].dynBal.U + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[6].dynBal.U + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[7].dynBal.U + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[8].dynBal.U + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[9].dynBal.U + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[10].dynBal.U + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[11].dynBal.U + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[12].dynBal.U + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[13].dynBal.U + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[14].dynBal.U + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[15].dynBal.U + enthalpyExchanger.membrane.heatTransfer.Ts[1] + enthalpyExchanger.membrane.heatTransfer.Ts[2] + enthalpyExchanger.membrane.heatTransfer.Ts[3] + enthalpyExchanger.membrane.heatTransfer.Ts[4] + enthalpyExchanger.membrane.heatTransfer.Ts[5] + enthalpyExchanger.membrane.heatTransfer.Ts[6] + enthalpyExchanger.membrane.heatTransfer.Ts[7] + enthalpyExchanger.membrane.heatTransfer.Ts[8] + enthalpyExchanger.membrane.heatTransfer.Ts[9] + enthalpyExchanger.membrane.heatTransfer.Ts[10] + enthalpyExchanger.membrane.heatTransfer.Ts[11] + enthalpyExchanger.membrane.heatTransfer.Ts[12] + enthalpyExchanger.membrane.heatTransfer.Ts[13] + enthalpyExchanger.membrane.heatTransfer.Ts[14] + enthalpyExchanger.membrane.heatTransfer.Ts[15] + senMasFraColIn.X + senMasFraColOut.X + senMasFraHotIn.X + senMasFraHotOut.X + senTemColIn.T + senTemColOut.T + senTemHotIn.T + senTemHotOut.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Examples.Test_EnthalpyExchanger.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp"); +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp: +The model has the same number of unknowns and equations: 522 +The model could not be deduced to be symbolically well-posed. +The model has + 514+pipeSupply.vol_b.dynBal.nPorts+pipeSupply.vol_a.dynBal.nPorts+ pipeReturn.vol_b.dynBal.nPorts+pipeReturn.vol_a.dynBal.nPorts +scalar unknowns and + 479+(if sourceIdeal.source.use_Xi_in then 1 else (if sourceIdeal.source.use_X_in then 0 else 1))+(if not sourceIdeal.source.use_p_in then 1 else 0)+2* sourceIdeal.source.nPorts+(if not sourceIdeal.source.use_T_in then 1 else 0)+ (if sourceIdeal.sink.use_Xi_in then 1 else (if sourceIdeal.sink.use_X_in then 0 else 1))+(if not sourceIdeal.sink.use_p_in then 1 else 0)+2*sourceIdeal.sink.nPorts +(if not sourceIdeal.sink.use_T_in then 1 else 0)+(if demand.sink.use_Xi_in then 1 else (if demand.sink.use_X_in then 0 else 1))+(if not demand.sink.use_m_flow_in then 1 else 0)+2*demand.sink.nPorts+(if not demand.sink.use_T_in then 1 else 0)+(if demand.source.use_Xi_in then 1 else ( if demand.source.use_X_in then 0 else 1))+(if not demand.source.use_m_flow_in then 1 else 0)+2*demand.source.nPorts+(if not demand.source.use_T_in then 1 else 0)+(if not pipeSupply.vol_b.dynBal.use_mWat_flow then 1 else 0)+3* pipeSupply.vol_b.dynBal.nPorts+(if not pipeSupply.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_a.dynBal.nPorts+(if not pipeReturn.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_b.dynBal.nPorts+(if not pipeReturn.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_a.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 522 +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDp.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDp.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp: +The DAE has 522 scalar unknowns and 522 scalar equations. + +Statistics + +Original Model + Number of components: 105 + Variables: 1376 + Constants: 25 (25 scalars) + Parameters: 625 (601 scalars) + Unknowns: 726 (538 scalars) + Differentiated variables: 15 scalars + Equations: 623 + Nontrivial: 504 +Translated Model + Constants: 457 scalars + Free parameters: 119 scalars + Parameter depending: 129 scalars + Continuous time states: 11 scalars + Time-varying variables: 123 scalars + Alias variables: 336 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + demand.senT_return.T + demand.senT_supply.T + pControl.I.y + pipeReturn.del.x + pipeReturn.timDel.x + pipeReturn.vol_a.dynBal.U + pipeReturn.vol_b.dynBal.U + pipeSupply.del.x + pipeSupply.timDel.x + pipeSupply.vol_a.dynBal.U + pipeSupply.vol_b.dynBal.U + + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp", stopTime=100000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp"); +Not possible to open file "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.mat": No such file or directory +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDp.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystem"); +Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystem: +The model has the same number of unknowns and equations: 367 +The model could not be deduced to be symbolically well-posed. +The model has + 361+combinedHeatPower.vol.dynBal.nPorts+size(combinedHeatPower.combiTable1Ds.columns, 1) +scalar unknowns and + 347+size(combinedHeatPower.combiTable1Ds.columns, 1)+2*source.nPorts+(if not source.use_m_flow_in then 1 else 0)+(if not source.use_T_in then 1 else 0)+( if not source.use_X_in then 1 else 0)+2*sink.nPorts+(if not sink.use_p_in then 1 else 0)+(if not sink.use_T_in then 1 else 0)+(if not sink.use_X_in then 1 else 0)+(if not combinedHeatPower.vol.dynBal.use_mWat_flow then 1 else 0)+3*combinedHeatPower.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 367 +Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystem successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystem.mos\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.BoilerCHP.Examples.CHPSystem\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.BoilerCHP.Examples.CHPSystem\\\");\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.BoilerCHP.Examples.CHPSystem.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystem.mos"); +simulateModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystem", tolerance=1e-06, stopTime=1200, method="dassl", resultFile="AixLib.Fluid.BoilerCHP.Examples.CHPSystem"); +Translation of AixLib.Fluid.BoilerCHP.Examples.CHPSystem: +The DAE has 367 scalar unknowns and 367 scalar equations. + +Statistics + +Original Model + Number of components: 105 + Variables: 786 + Constants: 8 (8 scalars) + Parameters: 360 (394 scalars) + Unknowns: 418 (371 scalars) + Differentiated variables: 8 scalars + Equations: 404 + Nontrivial: 360 +Translated Model + Constants: 177 scalars + Free parameters: 143 scalars + Parameter depending: 115 scalars + Continuous time states: 6 scalars + Time-varying variables: 112 scalars + Alias variables: 226 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {8, 9} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {5} + Sizes after manipulation of the linear systems: {0} + +Selected continuous time states +Statically selected continuous time states + combinedHeatPower.elControl.I.y + combinedHeatPower.senTRet.T + combinedHeatPower.senTSup.T + combinedHeatPower.thControl.PI.I.y + combinedHeatPower.thControl.PI1.I.y + combinedHeatPower.vol.dynBal.medium.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.BoilerCHP.Examples.CHPSystem.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst"); +Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst: +The model has the same number of unknowns and equations: 250 +The model could not be deduced to be symbolically well-posed. +The model has + 248+vol.dynBal.nPorts +scalar unknowns and + 237+(if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_p_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+ (if not dpControlled_dp.mov.vol.steBal.use_mWat_flow then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 250 +Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpConst.mos\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst\\\");\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpConst.mos"); +simulateModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst", startTime=0, stopTime=3600, tolerance=1e-6, method="dassl", resultFile="AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst"); +Translation of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst: +The DAE has 250 scalar unknowns and 250 scalar equations. + +Statistics + +Original Model + Number of components: 82 + Variables: 814 + Constants: 19 (19 scalars) + Parameters: 465 (949 scalars) + Unknowns: 330 (265 scalars) + Differentiated variables: 7 scalars + Equations: 284 + Nontrivial: 236 +Translated Model + Constants: 686 scalars + Free parameters: 51 scalars + Parameter depending: 271 scalars + Outputs: 1 scalars + Continuous time states: 5 scalars + Time-varying variables: 61 scalars + Alias variables: 164 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {3, 1} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {3, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + dpControlled_dp.mov.filter.s[1] + dpControlled_dp.mov.filter.s[2] + integrator.y + val.filter.s[1] + val.filter.s[2] + +Finished + = true + + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpConst.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageSimpleExample"); +Check of AixLib.Fluid.Storage.Examples.StorageSimpleExample: +The model has the same number of unknowns and equations: 964 +The model could not be deduced to be symbolically well-posed. +The model has + 938+storageSimple.layer[1].dynBal.nPorts+storageSimple.layer[2].dynBal.nPorts+ storageSimple.layer[3].dynBal.nPorts+storageSimple.layer_HE[1].dynBal.nPorts+ storageSimple.layer_HE[2].dynBal.nPorts+storageSimple.layer_HE[3].dynBal.nPorts +2*storageSimple.n+heatingRod.vol.dynBal.nPorts+simpleConsumer.volume.dynBal.nPorts +pumpGen.vol.dynBal.nPorts+pumpCon.vol.dynBal.nPorts +scalar unknowns and + 869+(if storageSimple.use_TOut then 2*storageSimple.n else 0)+(if pressureBoundary.use_Xi_in then 1 else (if pressureBoundary.use_X_in then 0 else 1))+(if not pressureBoundary.use_p_in then 1 else 0)+2*pressureBoundary.nPorts +(if not pressureBoundary.use_T_in then 1 else 0)+(if pressureBoundary1.use_Xi_in then 1 else (if pressureBoundary1.use_X_in then 0 else 1))+(if not pressureBoundary1.use_p_in then 1 else 0)+2*pressureBoundary1.nPorts+(if not pressureBoundary1.use_T_in then 1 else 0)+(if PIDHR.reset <> AixLib.Types.Reset. Input then 1 else 0)+(if PIDPumpGen.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if PIDPumpCon.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if not storageSimple.layer[1].dynBal.use_mWat_flow then 1 else 0)+3* storageSimple.layer[1].dynBal.nPorts+(if not storageSimple.layer[2].dynBal.use_mWat_flow then 1 else 0)+3*storageSimple.layer[2].dynBal.nPorts+(if not storageSimple.layer[3].dynBal.use_mWat_flow then 1 else 0)+3*storageSimple.layer[3].dynBal.nPorts +(if not storageSimple.layer_HE[1].dynBal.use_mWat_flow then 1 else 0)+3* storageSimple.layer_HE[1].dynBal.nPorts+(if not storageSimple.layer_HE[2].dynBal.use_mWat_flow then 1 else 0)+3*storageSimple.layer_HE[2].dynBal.nPorts+(if not storageSimple.layer_HE[3].dynBal.use_mWat_flow then 1 else 0)+3* storageSimple.layer_HE[3].dynBal.nPorts+(if not heatingRod.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatingRod.vol.dynBal.nPorts+(if not simpleConsumer.volume.dynBal.use_mWat_flow then 1 else 0)+3*simpleConsumer.volume.dynBal.nPorts+(if not pumpGen.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumpGen.vol.dynBal.nPorts+( if not pumpCon.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumpCon.vol.dynBal.nPorts +(if (if PIDHR.reset == AixLib.Types.Reset.Disabled then PIDHR.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if PIDHR.reset == AixLib.Types.Reset.Disabled then PIDHR.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if ( if PIDPumpGen.reset == AixLib.Types.Reset.Disabled then PIDPumpGen.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if PIDPumpGen.reset == AixLib.Types.Reset.Disabled then PIDPumpGen.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if ( if PIDPumpCon.reset == AixLib.Types.Reset.Disabled then PIDPumpCon.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if PIDPumpCon.reset == AixLib.Types.Reset.Disabled then PIDPumpCon.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 964 +Check of AixLib.Fluid.Storage.Examples.StorageSimpleExample successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSimpleExample.mos\",", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageSimpleExample\",", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageSimpleExample\\\");\",", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageSimpleExample.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSimpleExample.mos"); +simulateModel("AixLib.Fluid.Storage.Examples.StorageSimpleExample", tolerance=1e-6, stopTime=38200, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageSimpleExample"); +Translation of AixLib.Fluid.Storage.Examples.StorageSimpleExample: +The DAE has 964 scalar unknowns and 964 scalar equations. + +Statistics + +Original Model + Number of components: 247 + Variables: 2530 + Constants: 57 (57 scalars) + Parameters: 1181 (1670 scalars) + Unknowns: 1292 (1010 scalars) + Differentiated variables: 28 scalars + Equations: 1101 + Nontrivial: 860 +Translated Model + Constants: 1047 scalars + Free parameters: 186 scalars + Parameter depending: 627 scalars + Outputs: 1 scalars + Continuous time states: 17 scalars + Time-varying variables: 245 scalars + Alias variables: 632 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: {5, 7} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {5, 7} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + heatingRod.vol.dynBal.U + PIDHR.I.y + PIDPumpCon.I.y + PIDPumpGen.I.y + pumpCon.filter.s[1] + pumpCon.filter.s[2] + pumpCon.vol.dynBal.U + pumpGen.filter.s[1] + pumpGen.filter.s[2] + pumpGen.vol.dynBal.U + simpleConsumer.heatCapacitor.T + storageSimple.layer[1].dynBal.U + storageSimple.layer[2].dynBal.U + storageSimple.layer[3].dynBal.U + storageSimple.layer_HE[1].dynBal.U + storageSimple.layer_HE[2].dynBal.U + storageSimple.layer_HE[3].dynBal.U + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Storage.Examples.StorageSimpleExample.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar"); +Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar: +The model has the same number of unknowns and equations: 250 +The model could not be deduced to be symbolically well-posed. +The model has + 248+vol.dynBal.nPorts +scalar unknowns and + 237+(if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_p_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+ (if not dpControlled_dp.mov.vol.steBal.use_mWat_flow then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 250 +Check of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpVar.mos\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar\\\");\",", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/DpControlledMovers/Examples/DpVar.mos"); +simulateModel("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar", startTime=0, stopTime=3600, tolerance=1e-6, method="dassl", resultFile="AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar"); +Translation of AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar: +The DAE has 250 scalar unknowns and 250 scalar equations. + +Statistics + +Original Model + Number of components: 82 + Variables: 814 + Constants: 19 (19 scalars) + Parameters: 465 (949 scalars) + Unknowns: 330 (265 scalars) + Differentiated variables: 7 scalars + Equations: 284 + Nontrivial: 236 +Translated Model + Constants: 686 scalars + Free parameters: 51 scalars + Parameter depending: 271 scalars + Outputs: 1 scalars + Continuous time states: 5 scalars + Time-varying variables: 61 scalars + Alias variables: 164 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {3, 1} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {3, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + dpControlled_dp.mov.filter.s[1] + dpControlled_dp.mov.filter.s[2] + integrator.y + val.filter.s[1] + val.filter.s[2] + +Finished + = true + + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.DpControlledMovers.Examples.DpVar.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump"); +Check of AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump: +Warning: Members of records must be set in declaration, modified iceFacMea. + File: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/Examples/GeothermalHeatPump/GeothermalHeatPump.mo, line 40 + Context: AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.AixLib.Fluid.Examples.GeothermalHeatPump.BaseClasses.GeothermalHeatPumpControlledBase.heatPumpControlBus.iceFacMea +Original declaration of iceFacMea: + File: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Controls/Interfaces/VapourCompressionMachineControlBus.mo, line 42 + Context: AixLib.Controls.Interfaces.VapourCompressionMachineControlBus.iceFacMea +Warning: Redeclaration requires a subtype. + But missing component dp_start. + In redeclaration of PeakLoadDeviceModel. + File: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/Examples/GeothermalHeatPump/BaseClasses/GeothermalHeatPumpBase.mo, line 14 + Context: AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.PeakLoadDeviceModel +The model has the same number of unknowns and equations: 4648 +Check of AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Examples/GeothermalHeatPump.mos\",", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump\",", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump\\\");\",", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Examples/GeothermalHeatPump.mos"); +simulateModel("AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump", startTime=0, stopTime=86400, method="dassl", tolerance=1e-06, resultFile="AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump"); +Translation of AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump: +Warning: Members of records must be set in declaration, modified iceFacMea. + File: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/Examples/GeothermalHeatPump/GeothermalHeatPump.mo, line 40 + Context: AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.AixLib.Fluid.Examples.GeothermalHeatPump.BaseClasses.GeothermalHeatPumpControlledBase.heatPumpControlBus.iceFacMea +Original declaration of iceFacMea: + File: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Controls/Interfaces/VapourCompressionMachineControlBus.mo, line 42 + Context: AixLib.Controls.Interfaces.VapourCompressionMachineControlBus.iceFacMea +Warning: Redeclaration requires a subtype. + But missing component dp_start. + In redeclaration of PeakLoadDeviceModel. + File: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/Examples/GeothermalHeatPump/BaseClasses/GeothermalHeatPumpBase.mo, line 14 + Context: AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.PeakLoadDeviceModel +The DAE has 4648 scalar unknowns and 4648 scalar equations. +Sparse solver handling possible: false. +Due to flag Advanced.SparseActivate=false. +Model sparse and large enough: true. +Sparse solvers are available for dassl, lsodar, cvode, radau, esdirk*, sdirk* (using OpenMP, set number of cores with Advanced.NumberOfCores). +Warning: The conditions of the following assert statements are always false: +Warning: assert(heatPump.con.preDro.homotopyInitialization, "In GeothermalHeatPump.heatPump.con.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning); + The variable heatPump.con.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component heatPump.con.preDro.PartialResistance. +Warning: assert(heatPump.eva.preDro.homotopyInitialization, "In GeothermalHeatPump.heatPump.eva.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning); + The variable heatPump.eva.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component heatPump.eva.preDro.PartialResistance. + +Statistics + +Original Model + Number of components: 1044 + Variables: 12475 + Constants: 220 (220 scalars) + Parameters: 6082 (7303 scalars) + Unknowns: 6173 (4821 scalars) + Differentiated variables: 151 scalars + Equations: 4950 + Nontrivial: 3884 +Translated Model + Constants: 4229 scalars + Free parameters: 863 scalars + Parameter depending: 3037 scalars + Inputs: 1 scalars + Outputs: 14 scalars + Continuous time states: 113 scalars + Time-varying variables: 1192 scalars + Alias variables: 3023 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 3, 2, 2, 4, 3, 17, 2, 2, 2, 2, 2, 2, 2, 2, 3, 4, 2, 4, 3, 17, 4, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 8, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 8, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {12, 5, 12, 5, 6, 6, 6, 3, 1, 6, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1, 1, 1, 1, 0, 0, 1, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {12, 1, 5, 1, 12, 1, 5, 1, 3, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 2, 0, 1, 0, 1, 0, 1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + coldStorage.bottomCover.loadIns.T + coldStorage.bottomCover.loadWall.T + coldStorage.heatingCoil1.pipe[1].del.x + coldStorage.heatingCoil1.pipe[1].timDel.x + coldStorage.heatingCoil1.pipe[1].vol_a.dynBal.U + coldStorage.heatingCoil1.pipe[1].vol_b.dynBal.U + coldStorage.heatingCoil1.pipe[2].del.x + coldStorage.heatingCoil1.pipe[2].timDel.x + coldStorage.heatingCoil1.pipe[2].vol_a.dynBal.U + coldStorage.heatingCoil1.pipe[2].vol_b.dynBal.U + coldStorage.heatingCoil1.pipe[3].del.x + coldStorage.heatingCoil1.pipe[3].timDel.x + coldStorage.heatingCoil1.pipe[3].vol_a.dynBal.U + coldStorage.heatingCoil1.pipe[3].vol_b.dynBal.U + coldStorage.heatingCoil1.pipe[4].del.x + coldStorage.heatingCoil1.pipe[4].timDel.x + coldStorage.heatingCoil1.pipe[4].vol_a.dynBal.U + coldStorage.heatingCoil1.pipe[4].vol_b.dynBal.U + coldStorage.heatingCoil1.pipe[5].del.x + coldStorage.heatingCoil1.pipe[5].timDel.x + coldStorage.heatingCoil1.pipe[5].vol_a.dynBal.U + coldStorage.heatingCoil1.pipe[5].vol_b.dynBal.U + coldStorage.layer[1].dynBal.U + coldStorage.layer[2].dynBal.U + coldStorage.layer[3].dynBal.U + coldStorage.layer[4].dynBal.U + coldStorage.layer[5].dynBal.U + coldStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T + coldStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T + coldStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T + coldStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T + coldStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T + coldStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T + coldStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T + coldStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T + coldStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T + coldStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T + coldStorage.topCover.loadIns.T + coldStorage.topCover.loadWall.T + heatPump.con.vol.dynBal.U + heatPump.eva.vol.dynBal.U + heatPump.senT_a1.T + heatPump.senT_a2.T + heatPump.senT_b1.T + heatPump.senT_b2.T + heatStorage.bottomCover.loadIns.T + heatStorage.bottomCover.loadWall.T + heatStorage.heatingCoil1.pipe[1].del.x + heatStorage.heatingCoil1.pipe[1].timDel.x + heatStorage.heatingCoil1.pipe[1].vol_a.dynBal.U + heatStorage.heatingCoil1.pipe[1].vol_b.dynBal.U + heatStorage.heatingCoil1.pipe[2].del.x + heatStorage.heatingCoil1.pipe[2].timDel.x + heatStorage.heatingCoil1.pipe[2].vol_a.dynBal.U + heatStorage.heatingCoil1.pipe[2].vol_b.dynBal.U + heatStorage.heatingCoil1.pipe[3].del.x + heatStorage.heatingCoil1.pipe[3].timDel.x + heatStorage.heatingCoil1.pipe[3].vol_a.dynBal.U + heatStorage.heatingCoil1.pipe[3].vol_b.dynBal.U + heatStorage.heatingCoil1.pipe[4].del.x + heatStorage.heatingCoil1.pipe[4].timDel.x + heatStorage.heatingCoil1.pipe[4].vol_a.dynBal.U + heatStorage.heatingCoil1.pipe[4].vol_b.dynBal.U + heatStorage.heatingCoil1.pipe[5].del.x + heatStorage.heatingCoil1.pipe[5].timDel.x + heatStorage.heatingCoil1.pipe[5].vol_a.dynBal.U + heatStorage.heatingCoil1.pipe[5].vol_b.dynBal.U + heatStorage.layer[1].dynBal.U + heatStorage.layer[2].dynBal.U + heatStorage.layer[3].dynBal.U + heatStorage.layer[4].dynBal.U + heatStorage.layer[5].dynBal.U + heatStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T + heatStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T + heatStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T + heatStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T + heatStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T + heatStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T + heatStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T + heatStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T + heatStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T + heatStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T + heatStorage.topCover.loadIns.T + heatStorage.topCover.loadWall.T + peaLoaDev.boiler.internalControl.ControlerHeater.PI.I.y + peaLoaDev.boiler.internalControl.eEnergyMeter_P.q_joule + peaLoaDev.boiler.internalControl.eEnergyMeter_S.q_joule + peaLoaDev.boiler.senTRet.T + peaLoaDev.boiler.senTSup.T + peaLoaDev.boiler.vol.dynBal.U + pumpColdConsumer.filter.s[1] + pumpColdConsumer.filter.s[2] + pumpColdConsumer.vol.dynBal.U + pumpCondenser.filter.s[1] + pumpCondenser.filter.s[2] + pumpCondenser.vol.dynBal.U + pumpEvaporator.filter.s[1] + pumpEvaporator.filter.s[2] + pumpEvaporator.vol.dynBal.U + pumpGeothermalSource.filter.s[1] + pumpGeothermalSource.filter.s[2] + pumpGeothermalSource.vol.dynBal.U + pumpHeatConsumer.filter.s[1] + pumpHeatConsumer.filter.s[2] + pumpHeatConsumer.vol.dynBal.U + valveColdStorage.filter.s[1] + valveColdStorage.filter.s[2] + valveHeatSink.filter.s[1] + valveHeatSink.filter.s[2] + valveHeatSource.filter.s[1] + valveHeatSource.filter.s[2] + valveHeatStorage.filter.s[1] + valveHeatStorage.filter.s[2] + +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Examples.GeothermalHeatPump.GeothermalHeatPump.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPool"); +Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPool: +The model has the same number of unknowns and equations: 677 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 677 +Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPool successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPool.mos\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Pools.Examples.IndoorSwimmingPool\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Pools.Examples.IndoorSwimmingPool\\\");\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPool.mos"); +simulateModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPool", tolerance=1e-6, stopTime=604800, numberOfIntervals=0, outputInterval=900, method="CVode", resultFile="AixLib.Fluid.Pools.Examples.IndoorSwimmingPool"); +Translation of AixLib.Fluid.Pools.Examples.IndoorSwimmingPool: +The DAE has 677 scalar unknowns and 677 scalar equations. + +Statistics + +Original Model + Number of components: 161 + Variables: 1600 + Constants: 41 (41 scalars) + Parameters: 725 (917 scalars) + Unknowns: 834 (704 scalars) + Differentiated variables: 3 scalars + Equations: 700 + Nontrivial: 575 +Translated Model + Constants: 579 scalars + Free parameters: 125 scalars + Parameter depending: 369 scalars + Continuous time states: 3 scalars + Time-varying variables: 180 scalars + Alias variables: 409 scalars + Number of mixed real/discrete systems of equations: 1 + Sizes of linear systems of equations: {26} + Sizes after manipulation of the linear systems: {13} + Sizes of nonlinear systems of equations: {75, 1, 1} + Sizes after manipulation of the nonlinear systems: {16, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 74, 1} + Sizes after manipulation of the nonlinear systems: {0, 16, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + indoorSwimming.cirPump.filter.s[1] + indoorSwimming.cirPump.filter.s[2] + indoorSwimming.PI.I.y + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Pools.Examples.IndoorSwimmingPool.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances"); +Check of AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances: +The model has the same number of unknowns and equations: 60 +The model could not be deduced to be symbolically well-posed. +The model has + 60 +scalar unknowns and + 48+(if sou1.use_Xi_in then 1 else (if sou1.use_X_in then 0 else 1))+(if not sou1.use_p_in then 1 else 0)+2*sou1.nPorts+(if not sou1.use_T_in then 1 else 0) +(if sin1.use_Xi_in then 1 else (if sin1.use_X_in then 0 else 1))+(if not sin1.use_p_in then 1 else 0)+2*sin1.nPorts+(if not sin1.use_T_in then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 60 +Check of AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/CompareFixedResistances.mos\",", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances\",", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances\\\");\",", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/FixedResistances/Examples/CompareFixedResistances.mos"); +simulateModel("AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances", stopTime=3600, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances"); +Translation of AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances: +The DAE has 60 scalar unknowns and 60 scalar equations. + +Statistics + +Original Model + Number of components: 12 + Variables: 181 + Constants: 6 (6 scalars) + Parameters: 87 (85 scalars) + Unknowns: 88 (60 scalars) + Equations: 88 + Nontrivial: 81 +Translated Model + Constants: 66 scalars + Free parameters: 22 scalars + Parameter depending: 9 scalars + Time-varying variables: 7 scalars + Alias variables: 47 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.FixedResistances.Examples.CompareFixedResistances.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta"); +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta: +The model has the same number of unknowns and equations: 187 +The model could not be deduced to be symbolically well-posed. +The model has + 185+pip.vol.dynBal.nPorts +scalar unknowns and + 171+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if not pip.vol.dynBal.use_mWat_flow then 1 else 0)+3* pip.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 187 +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeZeta.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeZeta.mos"); +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta", stopTime=1000, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta: +The DAE has 187 scalar unknowns and 187 scalar equations. + +Statistics + +Original Model + Number of components: 34 + Variables: 537 + Constants: 10 (10 scalars) + Parameters: 262 (255 scalars) + Unknowns: 265 (193 scalars) + Differentiated variables: 6 scalars + Equations: 220 + Nontrivial: 186 +Translated Model + Constants: 189 scalars + Free parameters: 46 scalars + Parameter depending: 66 scalars + Continuous time states: 5 scalars + Time-varying variables: 39 scalars + Alias variables: 118 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + pip.plugFlowCore.del.x + pip.plugFlowCore.timDel.x + pip.vol.dynBal.U + senTemIn.T + senTemOut.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeZeta.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.HeatPumps.Examples.HeatPump"); +Check of AixLib.Fluid.HeatPumps.Examples.HeatPump: +The model has the same number of unknowns and equations: 634 +The model could not be deduced to be symbolically well-posed. +The model has + 626+heatPump.con.vol.dynBal.nPorts+heatPump.eva.vol.dynBal.nPorts+ pumSou.vol.dynBal.nPorts+Room.dynBal.nPorts +scalar unknowns and + 592+(if sourceSideMassFlowSource.use_Xi_in then 1 else (if sourceSideMassFlowSource.use_X_in then 0 else 1))+(if not sourceSideMassFlowSource.use_m_flow_in then 1 else 0) +2*sourceSideMassFlowSource.nPorts+(if not sourceSideMassFlowSource.use_T_in then 1 else 0)+(if sourceSideFixedBoundary.use_Xi_in then 1 else (if sourceSideFixedBoundary.use_X_in then 0 else 1))+(if not sourceSideFixedBoundary.use_p_in then 1 else 0)+2*sourceSideFixedBoundary.nPorts+(if not sourceSideFixedBoundary.use_T_in then 1 else 0)+(if sinkSideFixedBoundary.use_Xi_in then 1 else (if sinkSideFixedBoundary.use_X_in then 0 else 1))+(if not sinkSideFixedBoundary.use_p_in then 1 else 0)+2*sinkSideFixedBoundary.nPorts+(if not sinkSideFixedBoundary.use_T_in then 1 else 0)+(if not heatPump.con.vol.dynBal.use_mWat_flow then 1 else 0)+3 *heatPump.con.vol.dynBal.nPorts+(if not heatPump.eva.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatPump.eva.vol.dynBal.nPorts+(if not pumSou.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumSou.vol.dynBal.nPorts+(if not Room.dynBal.use_mWat_flow then 1 else 0)+3*Room.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 634 +Check of AixLib.Fluid.HeatPumps.Examples.HeatPump successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/HeatPumps/Examples/HeatPump.mos\",", "AixLib.Fluid.HeatPumps.Examples.HeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.HeatPumps.Examples.HeatPump\",", "AixLib.Fluid.HeatPumps.Examples.HeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.HeatPumps.Examples.HeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.HeatPumps.Examples.HeatPump\\\");\",", "AixLib.Fluid.HeatPumps.Examples.HeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.HeatPumps.Examples.HeatPump.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.HeatPumps.Examples.HeatPump.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/HeatPumps/Examples/HeatPump.mos"); +simulateModel("AixLib.Fluid.HeatPumps.Examples.HeatPump", tolerance=1e-6, stopTime=3600, method="dassl", resultFile="AixLib.Fluid.HeatPumps.Examples.HeatPump"); +Translation of AixLib.Fluid.HeatPumps.Examples.HeatPump: +The DAE has 634 scalar unknowns and 634 scalar equations. +Warning: The conditions of the following assert statements are always false: +Warning: assert(heatPump.con.preDro.homotopyInitialization, "In HeatPump.heatPump.con.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning); + The variable heatPump.con.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component heatPump.con.preDro.PartialResistance. +Warning: assert(heatPump.eva.preDro.homotopyInitialization, "In HeatPump.heatPump.eva.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning); + The variable heatPump.eva.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component heatPump.eva.preDro.PartialResistance. + +Statistics + +Original Model + Number of components: 164 + Variables: 1624 + Constants: 27 (27 scalars) + Parameters: 761 (1295 scalars) + Unknowns: 836 (659 scalars) + Differentiated variables: 15 scalars + Equations: 723 + Nontrivial: 603 +Translated Model + Constants: 697 scalars + Free parameters: 238 scalars + Parameter depending: 497 scalars + Outputs: 11 scalars + Continuous time states: 11 scalars + Time-varying variables: 127 scalars + Alias variables: 422 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + heatPump.con.vol.dynBal.U + heatPump.eva.vol.dynBal.U + heatPump.senT_a1.T + heatPump.senT_a2.T + heatPump.senT_b1.T + heatPump.senT_b2.T + pumSou.filter.s[1] + pumSou.filter.s[2] + pumSou.vol.dynBal.U + Room.dynBal.U + senTAct.T + +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.HeatPumps.Examples.HeatPump.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric"); +Check of AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric: +Warning: Non-literal value. +In nominal attribute for boiGen.preDro.m_flow. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class boiGen.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +Warning: Non-literal value. +In nominal attribute for boiGen.preDro.dp. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class boiGen.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +The model has the same number of unknowns and equations: 281 +The model could not be deduced to be symbolically well-posed. +The model has + 255+boiGen.vol.dynBal.nPorts+2*boiGen.offDesignOperation.multiplex4.n1+2* boiGen.offDesignOperation.multiplex4.n2+2*boiGen.offDesignOperation.multiplex4.n3 +2*boiGen.offDesignOperation.multiplex4.n4+boiGen.offDesignOperation.boilerEffciency.nin +2*boiGen.designOperation.multiplex4.n1+2*boiGen.designOperation.multiplex4.n2 +2*boiGen.designOperation.multiplex4.n3+2*boiGen.designOperation.multiplex4.n4 +boiGen.designOperation.boilerEffciency.nin +scalar unknowns and + 246+2*(boiGen.offDesignOperation.multiplex4.n1+boiGen.offDesignOperation.multiplex4.n2 +boiGen.offDesignOperation.multiplex4.n3+boiGen.offDesignOperation.multiplex4.n4 +boiGen.designOperation.multiplex4.n1+boiGen.designOperation.multiplex4.n2+ boiGen.designOperation.multiplex4.n3+boiGen.designOperation.multiplex4.n4+ source.nPorts)+(if not source.use_m_flow_in then 1 else 0)+(if not source.use_T_in then 1 else 0)+(if not source.use_X_in then 1 else 0)+2* sink.nPorts+(if not sink.use_p_in then 1 else 0)+(if not sink.use_T_in then 1 else 0)+(if not sink.use_X_in then 1 else 0)+(if conPID.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if not boiGen.vol.dynBal.use_mWat_flow then 1 else 0)+3*boiGen.vol.dynBal.nPorts+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 281 +Check of AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric successful. +Warning: WARNINGS have been issued. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/BoilerGeneric.mos\",", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric\",", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric\\\");\",", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/BoilerGeneric.mos"); +simulateModel("AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric", tolerance=1e-06, stopTime=1200, method="dassl", resultFile="AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric"); +Translation of AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric: +Warning: Non-literal value. +In nominal attribute for boiGen.preDro.m_flow. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class boiGen.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +Warning: Non-literal value. +In nominal attribute for boiGen.preDro.dp. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class boiGen.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-1-nf55iuop/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +The DAE has 281 scalar unknowns and 281 scalar equations. + +Statistics + +Original Model + Number of components: 69 + Variables: 558 + Constants: 6 (6 scalars) + Parameters: 250 (249 scalars) + Unknowns: 302 (285 scalars) + Differentiated variables: 6 scalars + Equations: 300 + Nontrivial: 247 +Translated Model + Constants: 183 scalars + Free parameters: 58 scalars + Parameter depending: 78 scalars + Outputs: 7 scalars + Continuous time states: 4 scalars + Time-varying variables: 43 scalars + Alias variables: 178 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + boiGen.senTRet.T + boiGen.senTSup.T + boiGen.vol.dynBal.U + conPID.I.y + +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.BoilerCHP.Examples.BoilerGeneric.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageBoiler"); +Check of AixLib.Fluid.Storage.Examples.StorageBoiler: +The model has the same number of unknowns and equations: 3241 +Check of AixLib.Fluid.Storage.Examples.StorageBoiler successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageBoiler.mos\",", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageBoiler\",", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageBoiler\\\");\",", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageBoiler.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageBoiler.mos"); +simulateModel("AixLib.Fluid.Storage.Examples.StorageBoiler", tolerance=1e-6, stopTime=86400, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageBoiler"); +Translation of AixLib.Fluid.Storage.Examples.StorageBoiler: +The DAE has 3241 scalar unknowns and 3241 scalar equations. + +Statistics + +Original Model + Number of components: 651 + Variables: 8627 + Constants: 159 (159 scalars) + Parameters: 4092 (4095 scalars) + Unknowns: 4376 (3344 scalars) + Differentiated variables: 106 scalars + Equations: 3314 + Nontrivial: 2545 +Translated Model + Constants: 2850 scalars + Free parameters: 287 scalars + Parameter depending: 1523 scalars + Continuous time states: 76 scalars + Time-varying variables: 843 scalars + Alias variables: 2095 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {22, 1, 6, 6, 6, 6, 6, 6, 6, 6, 6, 6, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {22, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + bufferStorage.bottomCover.loadIns.T + bufferStorage.bottomCover.loadWall.T + bufferStorage.heatingCoil1.pipe[1].del.x + bufferStorage.heatingCoil1.pipe[1].timDel.x + bufferStorage.heatingCoil1.pipe[1].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[1].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[2].del.x + bufferStorage.heatingCoil1.pipe[2].timDel.x + bufferStorage.heatingCoil1.pipe[2].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[2].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[3].del.x + bufferStorage.heatingCoil1.pipe[3].timDel.x + bufferStorage.heatingCoil1.pipe[3].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[3].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[4].del.x + bufferStorage.heatingCoil1.pipe[4].timDel.x + bufferStorage.heatingCoil1.pipe[4].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[4].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[5].del.x + bufferStorage.heatingCoil1.pipe[5].timDel.x + bufferStorage.heatingCoil1.pipe[5].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[5].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[6].del.x + bufferStorage.heatingCoil1.pipe[6].timDel.x + bufferStorage.heatingCoil1.pipe[6].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[6].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[7].del.x + bufferStorage.heatingCoil1.pipe[7].timDel.x + bufferStorage.heatingCoil1.pipe[7].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[7].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[8].del.x + bufferStorage.heatingCoil1.pipe[8].timDel.x + bufferStorage.heatingCoil1.pipe[8].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[8].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[9].del.x + bufferStorage.heatingCoil1.pipe[9].timDel.x + bufferStorage.heatingCoil1.pipe[9].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[9].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[10].del.x + bufferStorage.heatingCoil1.pipe[10].timDel.x + bufferStorage.heatingCoil1.pipe[10].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[10].vol_b.dynBal.U + bufferStorage.layer[1].dynBal.U + bufferStorage.layer[2].dynBal.U + bufferStorage.layer[3].dynBal.U + bufferStorage.layer[4].dynBal.U + bufferStorage.layer[5].dynBal.U + bufferStorage.layer[6].dynBal.U + bufferStorage.layer[7].dynBal.U + bufferStorage.layer[8].dynBal.U + bufferStorage.layer[9].dynBal.U + bufferStorage.layer[10].dynBal.U + bufferStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[6].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[6].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[7].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[7].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[8].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[8].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[9].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[9].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[10].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[10].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.topCover.loadIns.T + bufferStorage.topCover.loadWall.T + pump.filter.s[1] + pump.filter.s[2] + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Storage.Examples.StorageBoiler.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.HeatExchangers.Examples.HeatingRod"); +Check of AixLib.Fluid.HeatExchangers.Examples.HeatingRod: +The model has the same number of unknowns and equations: 327 +The model could not be deduced to be symbolically well-posed. +The model has + 322+vol.dynBal.nPorts+heatingRod.vol.dynBal.nPorts +scalar unknowns and + 301+(if conPI.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if bou.use_Xi_in then 1 else (if bou.use_X_in then 0 else 1))+(if not bou.use_p_in then 1 else 0)+2*bou.nPorts+(if not bou.use_T_in then 1 else 0)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts+(if not mov.vol.steBal.use_mWat_flow then 1 else 0)+(if (if conPI.reset == AixLib.Types.Reset.Disabled then conPI.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPI.reset == AixLib.Types.Reset.Disabled then conPI.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if not heatingRod.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatingRod.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 327 +Check of AixLib.Fluid.HeatExchangers.Examples.HeatingRod successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/HeatExchangers/Examples/HeatingRod.mos\",", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.HeatExchangers.Examples.HeatingRod\",", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.HeatExchangers.Examples.HeatingRod\\\");\",", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.HeatExchangers.Examples.HeatingRod.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/HeatExchangers/Examples/HeatingRod.mos"); +simulateModel("AixLib.Fluid.HeatExchangers.Examples.HeatingRod", stopTime=172800, method="Radau", tolerance=1e-6, resultFile="AixLib.Fluid.HeatExchangers.Examples.HeatingRod"); +Translation of AixLib.Fluid.HeatExchangers.Examples.HeatingRod: +The DAE has 327 scalar unknowns and 327 scalar equations. + +Statistics + +Original Model + Number of components: 93 + Variables: 927 + Constants: 21 (21 scalars) + Parameters: 472 (578 scalars) + Unknowns: 434 (342 scalars) + Differentiated variables: 8 scalars + Equations: 376 + Nontrivial: 305 +Translated Model + Constants: 397 scalars + Free parameters: 66 scalars + Parameter depending: 209 scalars + Outputs: 2 scalars + Continuous time states: 6 scalars + Time-varying variables: 79 scalars + Alias variables: 190 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + conPI.I.y + heatingRod.vol.dynBal.U + mov.filter.s[1] + mov.filter.s[2] + THeaOut.T + vol.dynBal.U + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.HeatExchangers.Examples.HeatingRod.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem"); +Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem: +The model has the same number of unknowns and equations: 733 +The model has the same number of unknowns and equations +for the given numerical settings of parameters: 733 +Check of AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPoolExternalHeatingSystem.mos\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem\\\");\",", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Pools/Examples/IndoorSwimmingPoolExternalHeatingSystem.mos"); +simulateModel("AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem", tolerance=1e-6, stopTime=604800, numberOfIntervals=0, outputInterval=900, method="CVode", resultFile="AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem"); +Translation of AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem: +The DAE has 733 scalar unknowns and 733 scalar equations. + +Statistics + +Original Model + Number of components: 171 + Variables: 1742 + Constants: 45 (45 scalars) + Parameters: 777 (964 scalars) + Unknowns: 920 (764 scalars) + Differentiated variables: 3 scalars + Equations: 763 + Nontrivial: 619 +Translated Model + Constants: 629 scalars + Free parameters: 133 scalars + Parameter depending: 374 scalars + Continuous time states: 3 scalars + Time-varying variables: 191 scalars + Alias variables: 446 scalars + Number of mixed real/discrete systems of equations: 1 + Sizes of linear systems of equations: {26} + Sizes after manipulation of the linear systems: {13} + Sizes of nonlinear systems of equations: {79, 1, 1} + Sizes after manipulation of the nonlinear systems: {17, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 78, 1} + Sizes after manipulation of the nonlinear systems: {0, 17, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + indoorSwimming.cirPump.filter.s[1] + indoorSwimming.cirPump.filter.s[2] + PI.I.y + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Pools.Examples.IndoorSwimmingPoolExternalHeatingSystem.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageSolarCollector"); +Check of AixLib.Fluid.Storage.Examples.StorageSolarCollector: +The model has the same number of unknowns and equations: 3387 +Check of AixLib.Fluid.Storage.Examples.StorageSolarCollector successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSolarCollector.mos\",", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageSolarCollector\",", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageSolarCollector\\\");\",", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageSolarCollector.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageSolarCollector.mos"); +simulateModel("AixLib.Fluid.Storage.Examples.StorageSolarCollector", tolerance=1e-6, stopTime=172800, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageSolarCollector"); +Translation of AixLib.Fluid.Storage.Examples.StorageSolarCollector: +The DAE has 3387 scalar unknowns and 3387 scalar equations. + +Statistics + +Original Model + Number of components: 688 + Variables: 8995 + Constants: 163 (163 scalars) + Parameters: 4276 (4349 scalars) + Unknowns: 4556 (3492 scalars) + Differentiated variables: 114 scalars + Equations: 3534 + Nontrivial: 2710 +Translated Model + Constants: 2921 scalars + Free parameters: 420 scalars + Parameter depending: 1577 scalars + Continuous time states: 83 scalars + Time-varying variables: 870 scalars + Alias variables: 2216 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4, 3, 3, 2, 2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {24, 1, 6, 6, 6, 6, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {24, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 0, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + bufferStorage.bottomCover.loadIns.T + bufferStorage.bottomCover.loadWall.T + bufferStorage.heatingCoil1.pipe[1].del.x + bufferStorage.heatingCoil1.pipe[1].timDel.x + bufferStorage.heatingCoil1.pipe[1].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[1].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[2].del.x + bufferStorage.heatingCoil1.pipe[2].timDel.x + bufferStorage.heatingCoil1.pipe[2].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[2].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[3].del.x + bufferStorage.heatingCoil1.pipe[3].timDel.x + bufferStorage.heatingCoil1.pipe[3].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[3].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[4].del.x + bufferStorage.heatingCoil1.pipe[4].timDel.x + bufferStorage.heatingCoil1.pipe[4].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[4].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[5].del.x + bufferStorage.heatingCoil1.pipe[5].timDel.x + bufferStorage.heatingCoil1.pipe[5].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[5].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[6].del.x + bufferStorage.heatingCoil1.pipe[6].timDel.x + bufferStorage.heatingCoil1.pipe[6].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[6].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[7].del.x + bufferStorage.heatingCoil1.pipe[7].timDel.x + bufferStorage.heatingCoil1.pipe[7].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[7].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[8].del.x + bufferStorage.heatingCoil1.pipe[8].timDel.x + bufferStorage.heatingCoil1.pipe[8].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[8].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[9].del.x + bufferStorage.heatingCoil1.pipe[9].timDel.x + bufferStorage.heatingCoil1.pipe[9].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[9].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[10].del.x + bufferStorage.heatingCoil1.pipe[10].timDel.x + bufferStorage.heatingCoil1.pipe[10].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[10].vol_b.dynBal.U + bufferStorage.layer[1].dynBal.U + bufferStorage.layer[2].dynBal.U + bufferStorage.layer[3].dynBal.U + bufferStorage.layer[4].dynBal.U + bufferStorage.layer[5].dynBal.U + bufferStorage.layer[6].dynBal.U + bufferStorage.layer[7].dynBal.U + bufferStorage.layer[8].dynBal.U + bufferStorage.layer[9].dynBal.U + bufferStorage.layer[10].dynBal.U + bufferStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[6].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[6].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[7].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[7].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[8].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[8].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[9].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[9].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[10].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[10].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.topCover.loadIns.T + bufferStorage.topCover.loadWall.T + PI.I.y + pump.filter.s[1] + pump.filter.s[2] + solarThermal.senTRet.T + solarThermal.senTSup.T + solarThermal.vol.dynBal.U + temperatureSensor.T + valve.filter.s[1] + valve.filter.s[2] + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Storage.Examples.StorageSolarCollector.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass"); +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass: +The model has the same number of unknowns and equations: 572 +The model could not be deduced to be symbolically well-posed. +The model has + 562+demand.vol.dynBal.nPorts+pipeSupply.vol_b.dynBal.nPorts+pipeSupply.vol_a.dynBal.nPorts +pipeReturn.vol_b.dynBal.nPorts+pipeReturn.vol_a.dynBal.nPorts +scalar unknowns and + 522+(if sourceIdeal.source.use_Xi_in then 1 else (if sourceIdeal.source.use_X_in then 0 else 1))+(if not sourceIdeal.source.use_p_in then 1 else 0)+2* sourceIdeal.source.nPorts+(if not sourceIdeal.source.use_T_in then 1 else 0)+ (if sourceIdeal.sink.use_Xi_in then 1 else (if sourceIdeal.sink.use_X_in then 0 else 1))+(if not sourceIdeal.sink.use_p_in then 1 else 0)+2*sourceIdeal.sink.nPorts +(if not sourceIdeal.sink.use_T_in then 1 else 0)+(if demand.sink.use_Xi_in then 1 else (if demand.sink.use_X_in then 0 else 1))+(if not demand.sink.use_m_flow_in then 1 else 0)+2*demand.sink.nPorts+(if not demand.sink.use_T_in then 1 else 0)+(if demand.source.use_Xi_in then 1 else ( if demand.source.use_X_in then 0 else 1))+(if not demand.source.use_m_flow_in then 1 else 0)+2*demand.source.nPorts+(if not demand.source.use_T_in then 1 else 0)+(if not demand.vol.dynBal.use_mWat_flow then 1 else 0)+3* demand.vol.dynBal.nPorts+(if not pipeSupply.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_b.dynBal.nPorts+(if not pipeSupply.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_a.dynBal.nPorts+(if not pipeReturn.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_b.dynBal.nPorts+(if not pipeReturn.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_a.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 572 +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass: +The DAE has 572 scalar unknowns and 572 scalar equations. + +Statistics + +Original Model + Number of components: 114 + Variables: 1506 + Constants: 29 (29 scalars) + Parameters: 675 (646 scalars) + Unknowns: 802 (590 scalars) + Differentiated variables: 17 scalars + Equations: 680 + Nontrivial: 543 +Translated Model + Constants: 509 scalars + Free parameters: 121 scalars + Parameter depending: 138 scalars + Continuous time states: 12 scalars + Time-varying variables: 132 scalars + Alias variables: 365 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + demand.senT_return.T + demand.senT_supply.T + demand.vol.dynBal.U + pControl.I.y + pipeReturn.del.x + pipeReturn.timDel.x + pipeReturn.vol_a.dynBal.U + pipeReturn.vol_b.dynBal.U + pipeSupply.del.x + pipeSupply.timDel.x + pipeSupply.vol_a.dynBal.U + pipeSupply.vol_b.dynBal.U + + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass", stopTime=100000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass"); +Not possible to open file "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.mat": No such file or directory +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopVarTSupplyDpFixedTempDifferenceBypass.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation"); +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation: +The model has the same number of unknowns and equations: 5514 +The model could not be deduced to be symbolically well-posed. +The model has + 3787+32*enthalpyExchanger.n+16*enthalpyExchanger.airDuct2.heatTransfer.n+18* enthalpyExchanger.airDuct2.massTransfer.n+16*enthalpyExchanger.airDuct1.heatTransfer.n +18*enthalpyExchanger.airDuct1.massTransfer.n+5*enthalpyExchanger.membrane.heatTransfer.n +enthalpyExchanger.membrane.massTransfer.n+2*enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts+max([size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size(bondaryOda.columns, 1); size( bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)]) +2*fan.vol.dynBal.nPorts+2*fan1.vol.dynBal.nPorts +scalar unknowns and + 3439+17*enthalpyExchanger.airDuct2.heatTransfer.n+19*enthalpyExchanger.airDuct2.massTransfer.n +3*(if enthalpyExchanger.couFloArr then 2*enthalpyExchanger.n else 0)+17* enthalpyExchanger.airDuct1.heatTransfer.n+19*enthalpyExchanger.airDuct1.massTransfer.n +7*enthalpyExchanger.membrane.heatTransfer.n+3*enthalpyExchanger.membrane.massTransfer.n +2*(if enthalpyExchanger.useConPer then 1 else 0)+32*enthalpyExchanger.n+(if souEta.use_Xi_in then 2 else (if souEta.use_X_in then 1 else 3))+3* souEta.nPorts+(if not souEta.use_p_in then 1 else 0)+(if not souEta.use_T_in then 1 else 0)+(if sinEha.use_Xi_in then 2 else (if sinEha.use_X_in then 1 else 3))+3*sinEha.nPorts+(if not sinEha.use_p_in then 1 else 0)+(if not sinEha.use_T_in then 1 else 0)+(if souOda.use_Xi_in then 2 else (if souOda.use_X_in then 1 else 3))+3*souOda.nPorts+(if not souOda.use_p_in then 1 else 0)+(if not souOda.use_T_in then 1 else 0)+(if sinSup.use_Xi_in then 2 else (if sinSup.use_X_in then 1 else 3))+3*sinSup.nPorts+(if not sinSup.use_p_in then 1 else 0)+(if not sinSup.use_T_in then 1 else 0)+max([ size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size( bondaryOda.columns, 1); size(bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)])+(if conPID.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if conPID1.reset <> AixLib.Types.Reset.Input then 1 else 0)+5 *enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +(if not fan.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan.vol.dynBal.nPorts+ (if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if not fan1.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan1.vol.dynBal.nPorts+( if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 5514 +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/DynamicValidation.mos\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation\\\");\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/DynamicValidation.mos"); +simulateModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation", stopTime=7200, numberOfIntervals=0, outputInterval=2, method="dassl",tolerance=1E-6, resultFile="AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation"); +Translation of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation: +The DAE has 5514 scalar unknowns and 5514 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + fan1.vol.p_start = fan1.p_start; + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial) then + if (fan.vol.dynBal.initialize_p) then + fan.vol.dynBal.medium.p = fan.vol.dynBal.p_start; + end if; + else + if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (fan.vol.dynBal.initialize_p) then + der(fan.vol.dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + fan.p_start(start = 101325) + fan1.p_start(start = 101325) + sinEha.p(start = 101325) + sinSup.p(start = 101325) + souEta.p(start = 101325) + souOda.p(start = 101325) + +The redundancies involve +initial equations: + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + souOda.p = fan.vol.dynBal.p_start; + souEta.p = fan1.vol.dynBal.p_start; + + +Statistics + +Original Model + Number of components: 678 + Variables: 7286 + Constants: 168 (168 scalars) + Parameters: 2808 (3271 scalars) + Unknowns: 4310 (5682 scalars) + Differentiated variables: 129 scalars + Equations: 2965 + Nontrivial: 2307 +Translated Model + Constants: 2677 scalars + Free parameters: 251 scalars + Parameter depending: 1421 scalars + Continuous time states: 97 scalars + Time-varying variables: 1772 scalars + Alias variables: 3000 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + conPID.I.y + conPID1.I.y + enthalpyExchanger.airDuct1.senRelHum.phi + enthalpyExchanger.airDuct1.senTem.T + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[1].dynBal.U + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[2].dynBal.U + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[3].dynBal.U + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[4].dynBal.U + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[5].dynBal.U + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[6].dynBal.U + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[7].dynBal.U + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[8].dynBal.U + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[9].dynBal.U + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[10].dynBal.U + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[11].dynBal.U + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[12].dynBal.U + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[13].dynBal.U + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[14].dynBal.U + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[15].dynBal.U + enthalpyExchanger.airDuct2.senRelHum.phi + enthalpyExchanger.airDuct2.senTem.T + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[1].dynBal.U + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[2].dynBal.U + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[3].dynBal.U + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[4].dynBal.U + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[5].dynBal.U + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[6].dynBal.U + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[7].dynBal.U + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[8].dynBal.U + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[9].dynBal.U + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[10].dynBal.U + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[11].dynBal.U + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[12].dynBal.U + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[13].dynBal.U + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[14].dynBal.U + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[15].dynBal.U + enthalpyExchanger.membrane.heatTransfer.Ts[1] + enthalpyExchanger.membrane.heatTransfer.Ts[2] + enthalpyExchanger.membrane.heatTransfer.Ts[3] + enthalpyExchanger.membrane.heatTransfer.Ts[4] + enthalpyExchanger.membrane.heatTransfer.Ts[5] + enthalpyExchanger.membrane.heatTransfer.Ts[6] + enthalpyExchanger.membrane.heatTransfer.Ts[7] + enthalpyExchanger.membrane.heatTransfer.Ts[8] + enthalpyExchanger.membrane.heatTransfer.Ts[9] + enthalpyExchanger.membrane.heatTransfer.Ts[10] + enthalpyExchanger.membrane.heatTransfer.Ts[11] + enthalpyExchanger.membrane.heatTransfer.Ts[12] + enthalpyExchanger.membrane.heatTransfer.Ts[13] + enthalpyExchanger.membrane.heatTransfer.Ts[14] + enthalpyExchanger.membrane.heatTransfer.Ts[15] + fan.filter.s[1] + fan.filter.s[2] + fan.vol.dynBal.medium.Xi[1] + fan.vol.dynBal.U + fan1.filter.s[1] + fan1.filter.s[2] + fan1.vol.dynBal.medium.Xi[1] + fan1.vol.dynBal.U + senMasFraEha.X + senMasFraEta.X + senMasFraOda.X + senMasFraSup.X + senTemEha.T + senTemEta.T + senTemOda.T + senTemSup.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.DynamicValidation.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded"); +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded: +The model has the same number of unknowns and equations: 256 +The model could not be deduced to be symbolically well-posed. +The model has + 254+pip.plugFlowPipeZeta.vol.dynBal.nPorts +scalar unknowns and + 240+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if not pip.plugFlowPipeZeta.vol.dynBal.use_mWat_flow then 1 else 0) +3*pip.plugFlowPipeZeta.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 256 +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeEmbedded.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/PlugFlowPipeEmbedded.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded: +The DAE has 256 scalar unknowns and 256 scalar equations. + +Statistics + +Original Model + Number of components: 53 + Variables: 739 + Constants: 11 (11 scalars) + Parameters: 390 (383 scalars) + Unknowns: 338 (264 scalars) + Differentiated variables: 9 scalars + Equations: 267 + Nontrivial: 229 +Translated Model + Constants: 224 scalars + Free parameters: 64 scalars + Parameter depending: 145 scalars + Continuous time states: 8 scalars + Time-varying variables: 57 scalars + Alias variables: 168 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2} + Sizes after manipulation of the linear systems: {0, 0} + Sizes of nonlinear systems of equations: {6} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {14} + Sizes after manipulation of the nonlinear systems: {6} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + pip.cylindricHeatTransfer_1.CylindricLoad1.heatCapacitor.T + pip.cylindricHeatTransfer_2.CylindricLoad1.heatCapacitor.T + pip.cylindricHeatTransfer_3.CylindricLoad1.heatCapacitor.T + pip.plugFlowPipeZeta.plugFlowCore.del.x + pip.plugFlowPipeZeta.plugFlowCore.timDel.x + pip.plugFlowPipeZeta.vol.dynBal.U + senTemIn.T + senTemOut.T + + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded", stopTime=1000, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded"); +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.PlugFlowPipeEmbedded.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled"); +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled: +The model has the same number of unknowns and equations: 156 +The model could not be deduced to be symbolically well-posed. +The model has + 144+2*(size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2) +pump.criticalDamping.n+pump.vol.dynBal.nPorts +scalar unknowns and + 134+2*size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2 +pump.criticalDamping.n+(if vessle.use_Xi_in then 1 else (if vessle.use_X_in then 0 else 1))+(if not vessle.use_p_in then 1 else 0)+2*vessle.nPorts+(if not vessle.use_T_in then 1 else 0)+(if not pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*pump.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 156 +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlled.mos\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled\\\");\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlled.mos"); +simulateModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled", tolerance=1e-6, stopTime=600.0, method="dassl", resultFile="AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled"); +Translation of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled: +The DAE has 156 scalar unknowns and 156 scalar equations. + +Statistics + +Original Model + Number of components: 35 + Variables: 388 + Constants: 15 (15 scalars) + Parameters: 177 (374 scalars) + Unknowns: 196 (160 scalars) + Differentiated variables: 6 scalars + Equations: 163 + Nontrivial: 137 +Translated Model + Constants: 242 scalars + Free parameters: 135 scalars + Parameter depending: 38 scalars + Outputs: 7 scalars + Continuous time states: 4 scalars + Time-varying variables: 37 scalars + Alias variables: 97 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + pump.criticalDamping.x[1] + pump.criticalDamping.x[2] + simpleValve.filter.s[1] + simpleValve.filter.s[2] + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlled.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Storage.Examples.StorageDetailedExample"); +Check of AixLib.Fluid.Storage.Examples.StorageDetailedExample: +The model has the same number of unknowns and equations: 2714 +Check of AixLib.Fluid.Storage.Examples.StorageDetailedExample successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageDetailedExample.mos\",", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Storage.Examples.StorageDetailedExample\",", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Storage.Examples.StorageDetailedExample\\\");\",", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Storage.Examples.StorageDetailedExample.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Storage/Examples/StorageDetailedExample.mos"); +simulateModel("AixLib.Fluid.Storage.Examples.StorageDetailedExample", tolerance=1e-6, stopTime=86400, method="dassl", resultFile="AixLib.Fluid.Storage.Examples.StorageDetailedExample"); +Translation of AixLib.Fluid.Storage.Examples.StorageDetailedExample: +The DAE has 2714 scalar unknowns and 2714 scalar equations. + +Statistics + +Original Model + Number of components: 532 + Variables: 7113 + Constants: 124 (124 scalars) + Parameters: 3345 (3234 scalars) + Unknowns: 3644 (2792 scalars) + Differentiated variables: 92 scalars + Equations: 2756 + Nontrivial: 2117 +Translated Model + Constants: 2426 scalars + Free parameters: 222 scalars + Parameter depending: 1324 scalars + Continuous time states: 66 scalars + Time-varying variables: 623 scalars + Alias variables: 1555 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 4, 3, 3, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {6, 6, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + bufferStorage.bottomCover.loadIns.T + bufferStorage.bottomCover.loadWall.T + bufferStorage.heatingCoil1.pipe[1].del.x + bufferStorage.heatingCoil1.pipe[1].timDel.x + bufferStorage.heatingCoil1.pipe[1].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[1].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[2].del.x + bufferStorage.heatingCoil1.pipe[2].timDel.x + bufferStorage.heatingCoil1.pipe[2].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[2].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[3].del.x + bufferStorage.heatingCoil1.pipe[3].timDel.x + bufferStorage.heatingCoil1.pipe[3].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[3].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[4].del.x + bufferStorage.heatingCoil1.pipe[4].timDel.x + bufferStorage.heatingCoil1.pipe[4].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[4].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[5].del.x + bufferStorage.heatingCoil1.pipe[5].timDel.x + bufferStorage.heatingCoil1.pipe[5].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[5].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[6].del.x + bufferStorage.heatingCoil1.pipe[6].timDel.x + bufferStorage.heatingCoil1.pipe[6].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[6].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[7].del.x + bufferStorage.heatingCoil1.pipe[7].timDel.x + bufferStorage.heatingCoil1.pipe[7].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[7].vol_b.dynBal.U + bufferStorage.heatingCoil1.pipe[8].del.x + bufferStorage.heatingCoil1.pipe[8].timDel.x + bufferStorage.heatingCoil1.pipe[8].vol_a.dynBal.U + bufferStorage.heatingCoil1.pipe[8].vol_b.dynBal.U + bufferStorage.layer[1].dynBal.U + bufferStorage.layer[2].dynBal.U + bufferStorage.layer[3].dynBal.U + bufferStorage.layer[4].dynBal.U + bufferStorage.layer[5].dynBal.U + bufferStorage.layer[6].dynBal.U + bufferStorage.layer[7].dynBal.U + bufferStorage.layer[8].dynBal.U + bufferStorage.layer[9].dynBal.U + bufferStorage.layer[10].dynBal.U + bufferStorage.storageMantle[1].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[1].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[2].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[2].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[3].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[3].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[4].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[4].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[5].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[5].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[6].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[6].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[7].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[7].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[8].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[8].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[9].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[9].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[10].Insulation.CylindricLoad1.heatCapacitor.T + bufferStorage.storageMantle[10].Wall.CylindricLoad1.heatCapacitor.T + bufferStorage.topCover.loadIns.T + bufferStorage.topCover.loadWall.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Storage.Examples.StorageDetailedExample.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV"); +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV: +The model has the same number of unknowns and equations: 220 +The model could not be deduced to be symbolically well-posed. +The model has + 208+2*(size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2) +pump.criticalDamping.n+pump.vol.dynBal.nPorts +scalar unknowns and + 198+2*size(pump.maxMinTable.columns, 1)+pump.deMultiplex2.n1+pump.deMultiplex2.n2 +pump.criticalDamping.n+(if vessle.use_Xi_in then 1 else (if vessle.use_X_in then 0 else 1))+(if not vessle.use_p_in then 1 else 0)+2*vessle.nPorts+(if not vessle.use_T_in then 1 else 0)+(if not pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*pump.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 220 +Check of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlledDpV.mos\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV\\\");\",", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Movers/PumpsPolynomialBased/Examples/PumpSpeedControlledDpV.mos"); +simulateModel("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV", tolerance=1e-6, stopTime=600.0, method="dassl", resultFile="AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV"); +Translation of AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV: +The DAE has 220 scalar unknowns and 220 scalar equations. + +Statistics + +Original Model + Number of components: 58 + Variables: 526 + Constants: 16 (16 scalars) + Parameters: 242 (586 scalars) + Unknowns: 268 (224 scalars) + Differentiated variables: 8 scalars + Equations: 228 + Nontrivial: 195 +Translated Model + Constants: 261 scalars + Free parameters: 310 scalars + Parameter depending: 59 scalars + Outputs: 4 scalars + Continuous time states: 6 scalars + Time-varying variables: 50 scalars + Alias variables: 146 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + ctrlDpVarN.PID.D.x + ctrlDpVarN.PID.I.y + pump.criticalDamping.x[1] + pump.criticalDamping.x[2] + simpleValve.filter.s[1] + simpleValve.filter.s[2] + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Movers.PumpsPolynomialBased.Examples.PumpSpeedControlledDpV.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot"); +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot: +The model has the same number of unknowns and equations: 699 +The model could not be deduced to be symbolically well-posed. +The model has + 691+pipeSupply.vol_b.dynBal.nPorts+pipeSupply.vol_a.dynBal.nPorts+ pipeReturn.vol_b.dynBal.nPorts+pipeReturn.vol_a.dynBal.nPorts +scalar unknowns and + 647+(if sourceIdeal.source.use_Xi_in then 1 else (if sourceIdeal.source.use_X_in then 0 else 1))+(if not sourceIdeal.source.use_p_in then 1 else 0)+2* sourceIdeal.source.nPorts+(if not sourceIdeal.source.use_T_in then 1 else 0)+ (if sourceIdeal.sink.use_Xi_in then 1 else (if sourceIdeal.sink.use_X_in then 0 else 1))+(if not sourceIdeal.sink.use_p_in then 1 else 0)+2*sourceIdeal.sink.nPorts +(if not sourceIdeal.sink.use_T_in then 1 else 0)+(if demand.sink.use_Xi_in then 1 else (if demand.sink.use_X_in then 0 else 1))+(if not demand.sink.use_m_flow_in then 1 else 0)+2*demand.sink.nPorts+(if not demand.sink.use_T_in then 1 else 0)+(if demand.source.use_Xi_in then 1 else ( if demand.source.use_X_in then 0 else 1))+(if not demand.source.use_m_flow_in then 1 else 0)+2*demand.source.nPorts+(if not demand.source.use_T_in then 1 else 0)+(if demand.sourceHeating.use_Xi_in then 1 else (if demand.sourceHeating.use_X_in then 0 else 1))+(if not demand.sourceHeating.use_m_flow_in then 1 else 0)+2* demand.sourceHeating.nPorts+(if not demand.sourceHeating.use_T_in then 1 else 0)+(if demand.sinkHeating.use_Xi_in then 1 else (if demand.sinkHeating.use_X_in then 0 else 1))+(if not demand.sinkHeating.use_p_in then 1 else 0)+2* demand.sinkHeating.nPorts+(if not demand.sinkHeating.use_T_in then 1 else 0)+ (if not demand.heaPum.eva.vol.steBal.use_mWat_flow then 1 else 0)+(if not pipeSupply.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeSupply.vol_b.dynBal.nPorts +(if not pipeSupply.vol_a.dynBal.use_mWat_flow then 1 else 0)+3* pipeSupply.vol_a.dynBal.nPorts+(if not pipeReturn.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_b.dynBal.nPorts+(if not pipeReturn.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*pipeReturn.vol_a.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 699 +Check of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopHeatPumpCarnot.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Demands/Examples/OpenLoopHeatPumpCarnot.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot: +The DAE has 699 scalar unknowns and 699 scalar equations. + +Statistics + +Original Model + Number of components: 145 + Variables: 1843 + Constants: 38 (38 scalars) + Parameters: 847 (817 scalars) + Unknowns: 958 (725 scalars) + Differentiated variables: 15 scalars + Equations: 799 + Nontrivial: 663 +Translated Model + Constants: 653 scalars + Free parameters: 145 scalars + Parameter depending: 165 scalars + Continuous time states: 11 scalars + Time-varying variables: 163 scalars + Alias variables: 454 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {13, 8} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {13, 8} + Sizes after manipulation of the nonlinear systems: {1, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + demand.senT_return.T + demand.senT_supply.T + pControl.I.y + pipeReturn.del.x + pipeReturn.timDel.x + pipeReturn.vol_a.dynBal.U + pipeReturn.vol_b.dynBal.U + pipeSupply.del.x + pipeSupply.timDel.x + pipeSupply.vol_a.dynBal.U + pipeSupply.vol_b.dynBal.U + + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot", stopTime=100000, method="dassl", tolerance=1e-006, resultFile="AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot"); +Not possible to open file "AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.mat": No such file or directory +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Demands.Examples.OpenLoopHeatPumpCarnot.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.Chillers.Examples.Chiller"); +Check of AixLib.Fluid.Chillers.Examples.Chiller: +The model has the same number of unknowns and equations: 625 +The model could not be deduced to be symbolically well-posed. +The model has + 617+chiller.con.vol.dynBal.nPorts+chiller.eva.vol.dynBal.nPorts+pumSou.vol.dynBal.nPorts +Room.dynBal.nPorts +scalar unknowns and + 583+(if sinkSideMassFlowSource.use_Xi_in then 1 else (if sinkSideMassFlowSource.use_X_in then 0 else 1))+(if not sinkSideMassFlowSource.use_m_flow_in then 1 else 0)+2 *sinkSideMassFlowSource.nPorts+(if not sinkSideMassFlowSource.use_T_in then 1 else 0)+(if sinkSideFixedBoundary.use_Xi_in then 1 else (if sinkSideFixedBoundary.use_X_in then 0 else 1))+(if not sinkSideFixedBoundary.use_p_in then 1 else 0)+2* sinkSideFixedBoundary.nPorts+(if not sinkSideFixedBoundary.use_T_in then 1 else 0)+(if sourceSideFixedBoundary.use_Xi_in then 1 else (if sourceSideFixedBoundary.use_X_in then 0 else 1))+(if not sourceSideFixedBoundary.use_p_in then 1 else 0)+2*sourceSideFixedBoundary.nPorts+(if not sourceSideFixedBoundary.use_T_in then 1 else 0)+(if not chiller.con.vol.dynBal.use_mWat_flow then 1 else 0)+3 *chiller.con.vol.dynBal.nPorts+(if not chiller.eva.vol.dynBal.use_mWat_flow then 1 else 0)+3*chiller.eva.vol.dynBal.nPorts+(if not pumSou.vol.dynBal.use_mWat_flow then 1 else 0)+3*pumSou.vol.dynBal.nPorts+(if not Room.dynBal.use_mWat_flow then 1 else 0)+3*Room.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 625 +Check of AixLib.Fluid.Chillers.Examples.Chiller successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/Chillers/Examples/Chiller.mos\",", "AixLib.Fluid.Chillers.Examples.Chiller.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.Chillers.Examples.Chiller\",", "AixLib.Fluid.Chillers.Examples.Chiller.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.Chillers.Examples.Chiller.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.Chillers.Examples.Chiller\\\");\",", "AixLib.Fluid.Chillers.Examples.Chiller.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.Chillers.Examples.Chiller.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.Chillers.Examples.Chiller.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/Chillers/Examples/Chiller.mos"); +simulateModel("AixLib.Fluid.Chillers.Examples.Chiller", tolerance=1e-6, stopTime=3600, method="dassl", resultFile="AixLib.Fluid.Chillers.Examples.Chiller"); +Translation of AixLib.Fluid.Chillers.Examples.Chiller: +The DAE has 625 scalar unknowns and 625 scalar equations. +Warning: The conditions of the following assert statements are always false: +Warning: assert(chiller.con.preDro.homotopyInitialization, "In Chiller.chiller.con.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning); + The variable chiller.con.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-3-lu4hlv37/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component chiller.con.preDro.PartialResistance. +Warning: assert(chiller.eva.preDro.homotopyInitialization, "In Chiller.chiller.eva.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning); + The variable chiller.eva.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-3-lu4hlv37/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component chiller.eva.preDro.PartialResistance. + +Statistics + +Original Model + Number of components: 163 + Variables: 1610 + Constants: 27 (27 scalars) + Parameters: 760 (1294 scalars) + Unknowns: 823 (650 scalars) + Differentiated variables: 15 scalars + Equations: 721 + Nontrivial: 602 +Translated Model + Constants: 696 scalars + Free parameters: 238 scalars + Parameter depending: 496 scalars + Continuous time states: 11 scalars + Time-varying variables: 123 scalars + Alias variables: 418 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: { } + Sizes after manipulation of the linear systems: { } + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + chiller.con.vol.dynBal.U + chiller.eva.vol.dynBal.U + chiller.senT_a1.T + chiller.senT_a2.T + chiller.senT_b1.T + chiller.senT_b2.T + pumSou.filter.s[1] + pumSou.filter.s[2] + pumSou.vol.dynBal.U + Room.dynBal.U + senTAct.T + +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.Chillers.Examples.Chiller.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl"); +Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl: +The model has the same number of unknowns and equations: 181 +The model could not be deduced to be symbolically well-posed. +The model has + 175+combinedHeatPower.vol.dynBal.nPorts+size(combinedHeatPower.combiTable1Ds.columns, 1) +scalar unknowns and + 161+size(combinedHeatPower.combiTable1Ds.columns, 1)+2*source.nPorts+(if not source.use_m_flow_in then 1 else 0)+(if not source.use_T_in then 1 else 0)+( if not source.use_X_in then 1 else 0)+2*sink.nPorts+(if not sink.use_p_in then 1 else 0)+(if not sink.use_T_in then 1 else 0)+(if not sink.use_X_in then 1 else 0)+(if not combinedHeatPower.vol.dynBal.use_mWat_flow then 1 else 0)+3*combinedHeatPower.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 181 +Check of AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystemNoControl.mos\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl\\\");\",", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/BoilerCHP/Examples/CHPSystemNoControl.mos"); +simulateModel("AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl", tolerance=1e-06, stopTime=300, method="dassl", resultFile="AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl"); +Translation of AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl: +The DAE has 181 scalar unknowns and 181 scalar equations. + +Statistics + +Original Model + Number of components: 38 + Variables: 432 + Constants: 5 (5 scalars) + Parameters: 195 (229 scalars) + Unknowns: 232 (185 scalars) + Differentiated variables: 5 scalars + Equations: 210 + Nontrivial: 170 +Translated Model + Constants: 143 scalars + Free parameters: 58 scalars + Parameter depending: 71 scalars + Continuous time states: 3 scalars + Time-varying variables: 38 scalars + Alias variables: 109 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: { } + Sizes after manipulation of the nonlinear systems: { } + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + combinedHeatPower.internalCapacity.T + combinedHeatPower.senTRet.T + combinedHeatPower.senTSup.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.BoilerCHP.Examples.CHPSystemNoControl.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation"); +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation: +The model has the same number of unknowns and equations: 5511 +The model could not be deduced to be symbolically well-posed. +The model has + 3783+32*enthalpyExchanger.n+16*enthalpyExchanger.airDuct2.heatTransfer.n+18* enthalpyExchanger.airDuct2.massTransfer.n+16*enthalpyExchanger.airDuct1.heatTransfer.n +18*enthalpyExchanger.airDuct1.massTransfer.n+5*enthalpyExchanger.membrane.heatTransfer.n +enthalpyExchanger.membrane.massTransfer.n+2*enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts +2*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts+2*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts+2*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts +2*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts+max([size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size(bondaryOda.columns, 1); size( bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)]) +2*fan.vol.dynBal.nPorts+2*fan1.vol.dynBal.nPorts +scalar unknowns and + 3435+17*enthalpyExchanger.airDuct2.heatTransfer.n+19*enthalpyExchanger.airDuct2.massTransfer.n +3*(if enthalpyExchanger.couFloArr then 2*enthalpyExchanger.n else 0)+17* enthalpyExchanger.airDuct1.heatTransfer.n+19*enthalpyExchanger.airDuct1.massTransfer.n +7*enthalpyExchanger.membrane.heatTransfer.n+3*enthalpyExchanger.membrane.massTransfer.n +2*(if enthalpyExchanger.useConPer then 1 else 0)+32*enthalpyExchanger.n+(if souEta.use_Xi_in then 2 else (if souEta.use_X_in then 1 else 3))+3* souEta.nPorts+(if not souEta.use_p_in then 1 else 0)+(if not souEta.use_T_in then 1 else 0)+(if sinEha.use_Xi_in then 2 else (if sinEha.use_X_in then 1 else 3))+3*sinEha.nPorts+(if not sinEha.use_p_in then 1 else 0)+(if not sinEha.use_T_in then 1 else 0)+(if souOda.use_Xi_in then 2 else (if souOda.use_X_in then 1 else 3))+3*souOda.nPorts+(if not souOda.use_p_in then 1 else 0)+(if not souOda.use_T_in then 1 else 0)+(if sinSup.use_Xi_in then 2 else (if sinSup.use_X_in then 1 else 3))+3*sinSup.nPorts+(if not sinSup.use_p_in then 1 else 0)+(if not sinSup.use_T_in then 1 else 0)+max([ size(bondaryEta.columns, 1); size(bondaryEta.offset, 1)])+max([size( bondaryOda.columns, 1); size(bondaryOda.offset, 1)])+max([size(Results.columns, 1); size(Results.offset, 1)])+(if conPID.reset <> AixLib.Types.Reset.Input then 1 else 0)+(if conPID1.reset <> AixLib.Types.Reset.Input then 1 else 0)+5 *enthalpyExchanger.airDuct2.vol[1].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[2].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[3].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[4].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[5].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[6].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[7].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[8].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[9].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[10].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[11].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[12].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[13].dynBal.nPorts+5*enthalpyExchanger.airDuct2.vol[14].dynBal.nPorts +5*enthalpyExchanger.airDuct2.vol[15].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[1].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[2].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[3].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[4].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[5].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[6].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[7].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[8].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[9].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[10].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[11].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[12].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[13].dynBal.nPorts +5*enthalpyExchanger.airDuct1.vol[14].dynBal.nPorts+5*enthalpyExchanger.airDuct1.vol[15].dynBal.nPorts +(if not fan.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan.vol.dynBal.nPorts+ (if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID.reset == AixLib.Types.Reset.Disabled then conPID.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0)+(if not fan1.vol.dynBal.use_mWat_flow then 1 else 0)+5*fan1.vol.dynBal.nPorts+( if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) <> AixLib.Types.Reset.Input then 1 else 0)+(if (if conPID1.reset == AixLib.Types.Reset.Disabled then conPID1.reset else AixLib.Types.Reset.Input) == AixLib.Types.Reset.Disabled then 1 else 0) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 5511 +Check of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/StaticValidation.mos\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation\\\");\",", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/MassExchangers/MembraneBasedEnthalpyExchangers/Validation/StaticValidation.mos"); +simulateModel("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation", stopTime=29600, numberOfIntervals=0, outputInterval=1, method="dassl",tolerance=1E-6, resultFile="AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation"); +Translation of AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation: +The DAE has 5511 scalar unknowns and 5511 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + fan1.vol.p_start = fan1.p_start; + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct2.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct2.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct2.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct2.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[1].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[1].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[2].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[2].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[3].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[3].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[3].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[3].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[4].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[4].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[4].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[4].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[5].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[5].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[5].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[5].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[6].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[6].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[6].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[6].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[7].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[7].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[7].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[7].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[8].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[8].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[8].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[8].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[9].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[9].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[9].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[9].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[10].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[10].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[10].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[10].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[11].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[11].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[11].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[11].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[12].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[12].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[12].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[12].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[13].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[13].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[13].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[13].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[14].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[14].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[14].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[14].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p = enthalpyExchanger.airDuct1.vol[15].dynBal.p_start; + end if; + else + if (enthalpyExchanger.airDuct1.vol[15].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial) then + if (enthalpyExchanger.airDuct1.vol[15].dynBal.initialize_p) then + der(enthalpyExchanger.airDuct1.vol[15].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial) then + if (fan.vol.dynBal.initialize_p) then + fan.vol.dynBal.medium.p = fan.vol.dynBal.p_start; + end if; + else + if (fan.vol.dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (fan.vol.dynBal.initialize_p) then + der(fan.vol.dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + fan.p_start(start = 101325) + fan1.p_start(start = 101325) + sinEha.p(start = 101325) + sinSup.p(start = 101325) + souEta.p(start = 101325) + souOda.p(start = 101325) + +The redundancies involve +initial equations: + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinSup.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + sinEha.p = 101325.0; + souOda.p = fan.vol.dynBal.p_start; + souEta.p = fan1.vol.dynBal.p_start; + + +Statistics + +Original Model + Number of components: 676 + Variables: 7282 + Constants: 168 (168 scalars) + Parameters: 2808 (3273 scalars) + Unknowns: 4306 (5679 scalars) + Differentiated variables: 129 scalars + Equations: 2961 + Nontrivial: 2303 +Translated Model + Constants: 2677 scalars + Free parameters: 252 scalars + Parameter depending: 1422 scalars + Continuous time states: 97 scalars + Time-varying variables: 1771 scalars + Alias variables: 2998 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3, 3} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes of nonlinear systems of equations: {1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 1} + Sizes after manipulation of the nonlinear systems: {0, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + conPID.I.y + conPID1.I.y + enthalpyExchanger.airDuct1.senRelHum.phi + enthalpyExchanger.airDuct1.senTem.T + enthalpyExchanger.airDuct1.vol[1].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[1].dynBal.U + enthalpyExchanger.airDuct1.vol[2].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[2].dynBal.U + enthalpyExchanger.airDuct1.vol[3].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[3].dynBal.U + enthalpyExchanger.airDuct1.vol[4].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[4].dynBal.U + enthalpyExchanger.airDuct1.vol[5].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[5].dynBal.U + enthalpyExchanger.airDuct1.vol[6].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[6].dynBal.U + enthalpyExchanger.airDuct1.vol[7].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[7].dynBal.U + enthalpyExchanger.airDuct1.vol[8].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[8].dynBal.U + enthalpyExchanger.airDuct1.vol[9].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[9].dynBal.U + enthalpyExchanger.airDuct1.vol[10].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[10].dynBal.U + enthalpyExchanger.airDuct1.vol[11].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[11].dynBal.U + enthalpyExchanger.airDuct1.vol[12].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[12].dynBal.U + enthalpyExchanger.airDuct1.vol[13].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[13].dynBal.U + enthalpyExchanger.airDuct1.vol[14].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[14].dynBal.U + enthalpyExchanger.airDuct1.vol[15].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct1.vol[15].dynBal.U + enthalpyExchanger.airDuct2.senRelHum.phi + enthalpyExchanger.airDuct2.senTem.T + enthalpyExchanger.airDuct2.vol[1].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[1].dynBal.U + enthalpyExchanger.airDuct2.vol[2].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[2].dynBal.U + enthalpyExchanger.airDuct2.vol[3].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[3].dynBal.U + enthalpyExchanger.airDuct2.vol[4].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[4].dynBal.U + enthalpyExchanger.airDuct2.vol[5].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[5].dynBal.U + enthalpyExchanger.airDuct2.vol[6].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[6].dynBal.U + enthalpyExchanger.airDuct2.vol[7].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[7].dynBal.U + enthalpyExchanger.airDuct2.vol[8].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[8].dynBal.U + enthalpyExchanger.airDuct2.vol[9].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[9].dynBal.U + enthalpyExchanger.airDuct2.vol[10].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[10].dynBal.U + enthalpyExchanger.airDuct2.vol[11].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[11].dynBal.U + enthalpyExchanger.airDuct2.vol[12].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[12].dynBal.U + enthalpyExchanger.airDuct2.vol[13].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[13].dynBal.U + enthalpyExchanger.airDuct2.vol[14].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[14].dynBal.U + enthalpyExchanger.airDuct2.vol[15].dynBal.medium.Xi[1] + enthalpyExchanger.airDuct2.vol[15].dynBal.U + enthalpyExchanger.membrane.heatTransfer.Ts[1] + enthalpyExchanger.membrane.heatTransfer.Ts[2] + enthalpyExchanger.membrane.heatTransfer.Ts[3] + enthalpyExchanger.membrane.heatTransfer.Ts[4] + enthalpyExchanger.membrane.heatTransfer.Ts[5] + enthalpyExchanger.membrane.heatTransfer.Ts[6] + enthalpyExchanger.membrane.heatTransfer.Ts[7] + enthalpyExchanger.membrane.heatTransfer.Ts[8] + enthalpyExchanger.membrane.heatTransfer.Ts[9] + enthalpyExchanger.membrane.heatTransfer.Ts[10] + enthalpyExchanger.membrane.heatTransfer.Ts[11] + enthalpyExchanger.membrane.heatTransfer.Ts[12] + enthalpyExchanger.membrane.heatTransfer.Ts[13] + enthalpyExchanger.membrane.heatTransfer.Ts[14] + enthalpyExchanger.membrane.heatTransfer.Ts[15] + fan.filter.s[1] + fan.filter.s[2] + fan.vol.dynBal.medium.Xi[1] + fan.vol.dynBal.U + fan1.filter.s[1] + fan1.filter.s[2] + fan1.vol.dynBal.medium.Xi[1] + fan1.vol.dynBal.U + senMasFraEha.X + senMasFraEta.X + senMasFraOda.X + senMasFraSup.X + senTemEha.T + senTemEta.T + senTemOda.T + senTemSup.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.MassExchangers.MembraneBasedEnthalpyExchangers.Validation.StaticValidation.translation.log"); = true + + +rCheck = checkModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe"); +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe: +The model has the same number of unknowns and equations: 804 +The model could not be deduced to be symbolically well-posed. +The model has + 796+pip.vol.dynBal.nPorts+pip1.vol.dynBal.nPorts+pip2.vol.dynBal.nPorts+ pip3.vol.dynBal.nPorts +scalar unknowns and + 740+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts+(if not sin.use_T_in then 1 else 0)+ (if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_m_flow_in then 1 else 0)+2*sou.nPorts+(if not sou.use_T_in then 1 else 0)+(if sin1.use_Xi_in then 1 else (if sin1.use_X_in then 0 else 1))+(if not sin1.use_p_in then 1 else 0)+2*sin1.nPorts+(if not sin1.use_T_in then 1 else 0)+(if sou1.use_Xi_in then 1 else (if sou1.use_X_in then 0 else 1))+(if not sou1.use_m_flow_in then 1 else 0)+2*sou1.nPorts+(if not sou1.use_T_in then 1 else 0)+(if sin2.use_Xi_in then 1 else (if sin2.use_X_in then 0 else 1)) +(if not sin2.use_p_in then 1 else 0)+2*sin2.nPorts+(if not sin2.use_T_in then 1 else 0)+(if sou2.use_Xi_in then 1 else (if sou2.use_X_in then 0 else 1)) +(if not sou2.use_m_flow_in then 1 else 0)+2*sou2.nPorts+(if not sou2.use_T_in then 1 else 0)+(if sin3.use_Xi_in then 1 else (if sin3.use_X_in then 0 else 1))+(if not sin3.use_p_in then 1 else 0)+2*sin3.nPorts+(if not sin3.use_T_in then 1 else 0)+(if sou3.use_Xi_in then 1 else (if sou3.use_X_in then 0 else 1))+(if not sou3.use_m_flow_in then 1 else 0)+2*sou3.nPorts+(if not sou3.use_T_in then 1 else 0)+(if not pip.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip.vol.dynBal.nPorts+(if not pip1.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip1.vol.dynBal.nPorts+(if not pip2.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip2.vol.dynBal.nPorts+(if not pip3.vol.dynBal.use_mWat_flow then 1 else 0)+3*pip3.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 804 +Check of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mos\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe\\\");\",", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Fluid/DistrictHeatingCooling/Pipes/Examples/DHCPipe.mos"); +translateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe"); +Translation of AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe: +The DAE has 804 scalar unknowns and 804 scalar equations. + +Statistics + +Original Model + Number of components: 144 + Variables: 2246 + Constants: 37 (37 scalars) + Parameters: 1101 (1073 scalars) + Unknowns: 1108 (828 scalars) + Differentiated variables: 33 scalars + Equations: 923 + Nontrivial: 790 +Translated Model + Constants: 721 scalars + Free parameters: 205 scalars + Parameter depending: 321 scalars + Continuous time states: 29 scalars + Time-varying variables: 177 scalars + Alias variables: 514 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2} + Sizes after manipulation of the linear systems: {0, 0} + Sizes of nonlinear systems of equations: {6} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + pip.Q_gai + pip.Q_los + pip.vol.dynBal.U + pip1.pipCor.del.x + pip1.pipCor.timDel.x + pip1.Q_gai + pip1.Q_los + pip1.vol.dynBal.U + pip2.cylHeaTra1.CylindricLoad1.heatCapacitor.T + pip2.cylHeaTra2.CylindricLoad1.heatCapacitor.T + pip2.cylHeaTra3.CylindricLoad1.heatCapacitor.T + pip2.pipCor.del.x + pip2.pipCor.timDel.x + pip2.Q_gai + pip2.Q_los + pip2.vol.dynBal.U + pip3.pipCor.del.x + pip3.pipCor.timDel.x + pip3.Q_gai + pip3.Q_los + pip3.vol.dynBal.U + senTemIn.T + senTemIn1.T + senTemIn2.T + senTemIn3.T + senTemOut.T + senTemOut1.T + senTemOut2.T + senTemOut3.T + + = true +simulateModel("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe", stopTime=3600, method="dassl", tolerance=1e-6, resultFile="AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe"); +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Fluid.DistrictHeatingCooling.Pipes.Examples.DHCPipe.translation.log"); \ No newline at end of file diff --git a/docs/issue1147_GenericBoiler/regression/Fluid/unitTests-dymola.log b/docs/issue1147_GenericBoiler/regression/Fluid/unitTests-dymola.log new file mode 100644 index 0000000000..826532da2e --- /dev/null +++ b/docs/issue1147_GenericBoiler/regression/Fluid/unitTests-dymola.log @@ -0,0 +1,10 @@ +Regression tests are only run for the following package: + AixLib.Fluid +*** Error: Fluid/BoilerCHP/Examples/CHPSystem.mos uses combinedHeatPower.senTHot.T which does not exist in AixLib.Fluid.BoilerCHP.Examples.CHPSystem.mat. + +Comparison files output by funnel are stored in the directory 'funnel_comp' of size 1.3 MB. +Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"' +to access a summary of the comparison results. + +Script that runs unit tests had 0 warnings and 1 errors. + diff --git a/docs/issue1147_GenericBoiler/regression/Systems/comparison-dymola.log b/docs/issue1147_GenericBoiler/regression/Systems/comparison-dymola.log new file mode 100644 index 0000000000..5db08129ea --- /dev/null +++ b/docs/issue1147_GenericBoiler/regression/Systems/comparison-dymola.log @@ -0,0 +1,1082 @@ +[ + { + "comparison": { + "file_name": "AixLib.Systems.ModularAHU.Examples.Heater.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Systems.ModularAHU.Examples.Heater.mat_ctrBasic.registerBus.TAirInMea", + "funnel_comp/AixLib.Systems.ModularAHU.Examples.Heater.mat_ctrBasic.registerBus.TAirOutMea", + "funnel_comp/AixLib.Systems.ModularAHU.Examples.Heater.mat_ctrBasic.registerBus.hydraulicBus.valveSet" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 0, + 1 + ], + "variables": [ + "ctrBasic.registerBus.TAirInMea", + "ctrBasic.registerBus.TAirOutMea", + "ctrBasic.registerBus.hydraulicBus.valveSet" + ], + "warnings": [ + null, + null, + null + ] + }, + "model": "AixLib.Systems.ModularAHU.Examples.Heater", + "simulation": { + "elapsed_time": 0.0229, + "final_time": 3600, + "jacobians": 31, + "start_time": 0, + "state_events": 0, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Systems.HydraulicModules.Example.Pump.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Pump.mat_hydraulicBus.TFwrdInMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Pump.mat_hydraulicBus.TFwrdOutMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Pump.mat_hydraulicBus.TRtrnInMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Pump.mat_hydraulicBus.TRtrnOutMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Pump.mat_hydraulicBus.VFlowInMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Pump.mat_hydraulicBus.VFlowOutMea" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1, + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 0, + 0, + 0, + 1, + 1 + ], + "variables": [ + "hydraulicBus.TFwrdInMea", + "hydraulicBus.TFwrdOutMea", + "hydraulicBus.TRtrnInMea", + "hydraulicBus.TRtrnOutMea", + "hydraulicBus.VFlowInMea", + "hydraulicBus.VFlowOutMea" + ], + "warnings": [ + null, + null, + null, + null, + null, + null + ] + }, + "model": "AixLib.Systems.HydraulicModules.Example.Pump", + "simulation": { + "elapsed_time": 0.0182, + "final_time": 800, + "jacobians": 67, + "start_time": 0, + "state_events": 1, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.TSupMea", + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.TRetMea", + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.Efficiency", + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.ThermalPower", + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.fuelPower" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 0, + 1, + 2, + 2 + ], + "variables": [ + "boilerControlBus.TSupMea", + "boilerControlBus.TRetMea", + "boilerControlBus.Efficiency", + "boilerControlBus.ThermalPower", + "boilerControlBus.fuelPower" + ], + "warnings": [ + null, + null, + null, + null, + null + ] + }, + "model": "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple", + "simulation": { + "elapsed_time": 0.0345, + "final_time": 84000, + "jacobians": 97, + "start_time": 0, + "state_events": 3, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Systems.HydraulicModules.Example.Injection.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Injection.mat_hydraulicBus.TFwrdInMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Injection.mat_hydraulicBus.TFwrdOutMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Injection.mat_hydraulicBus.TRtrnInMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Injection.mat_hydraulicBus.TRtrnOutMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Injection.mat_hydraulicBus.VFlowInMea", + "funnel_comp/AixLib.Systems.HydraulicModules.Example.Injection.mat_hydraulicBus.VFlowOutMea" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1, + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 0, + 0, + 0, + 1, + 1 + ], + "variables": [ + "hydraulicBus.TFwrdInMea", + "hydraulicBus.TFwrdOutMea", + "hydraulicBus.TRtrnInMea", + "hydraulicBus.TRtrnOutMea", + "hydraulicBus.VFlowInMea", + "hydraulicBus.VFlowOutMea" + ], + "warnings": [ + null, + null, + null, + null, + null, + null + ] + }, + "model": "AixLib.Systems.HydraulicModules.Example.Injection", + "simulation": { + "elapsed_time": 0.027, + "final_time": 800, + "jacobians": 55, + "start_time": 0, + "state_events": 0, + "success": true + } + }, + { + "comparison": { + "file_name": 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"funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.mat_combiTimeTable.y[8]", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.mat_Simulation_VF_in_m3h.y", + "funnel_comp/AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.mat_Simulation_VF_out_m3h.y" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 0, + 0, + 0, + 1, + 1, + 1, + 1, + 2, + 2, + 2, + 2 + ], + "variables": [ + "registerModule.registerBus.TAirInMea", + "registerModule.registerBus.TAirOutMea", + "combiTimeTable.y[6]", + "combiTimeTable.y[5]", + "combiTimeTable.y[3]", + "combiTimeTable.y[4]", + "registerModule.registerBus.hydraulicBus.TFwrdOutMea", + "registerModule.registerBus.hydraulicBus.TRtrnInMea", + "combiTimeTable.y[9]", + "combiTimeTable.y[8]", + "Simulation_VF_in_m3h.y", + "Simulation_VF_out_m3h.y" + ], + "warnings": [ + null, + null, + null, + null, + null, + null, + null, + null, + null, + null, + null, + null + ] + }, + "model": "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler", + "simulation": { + "elapsed_time": 2.56, + "final_time": 2700, + "jacobians": 11738, + "start_time": 0, + "state_events": 0, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.mat_genericAHU.genericAHUBus.TSupMea", + "funnel_comp/AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.mat_genericAHU.genericAHUBus.TOdaMea", + "funnel_comp/AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.mat_genericAHU.genericAHUBus.heaterBus.hydraulicBus.valveSet", + "funnel_comp/AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.mat_genericAHU.genericAHUBus.heaterBus.VFlowAirMea", + 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null, + null, + null + ] + }, + "model": "AixLib.Systems.HydraulicModules.Example.Throttle", + "simulation": { + "elapsed_time": 0.0121, + "final_time": 1000, + "jacobians": 43, + "start_time": 0, + "state_events": 0, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.mat", + "funnel_dirs": [ + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.mat_boilerControlBus.TSupMea", + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.mat_boilerControlBus.TRetMea", + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.mat_boilerControlBus.Efficiency", + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.mat_boilerControlBus.ThermalPower", + "funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.mat_boilerControlBus.fuelPower" + ], + "success_rate": 1.0, + "t_err_max": [ + 0.0, + 0.0, + 0.0, + 0.0, + 0.0 + ], + "test_passed": [ + 1, + 1, + 1, + 1, + 1 + ], + "var_groups": [ + 0, + 0, + 1, + 2, + 2 + ], + "variables": [ + "boilerControlBus.TSupMea", + "boilerControlBus.TRetMea", + "boilerControlBus.Efficiency", + "boilerControlBus.ThermalPower", + "boilerControlBus.fuelPower" + ], + "warnings": [ + null, + null, + null, + null, + null + ] + }, + "model": "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve", + "simulation": { + "elapsed_time": 0.0542, + "final_time": 84000, + "jacobians": 542, + "start_time": 0, + "state_events": 12, + "success": true + } + }, + { + "comparison": { + "file_name": "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.mat", + "funnel_dirs": [ + 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b/docs/issue1147_GenericBoiler/regression/Systems/funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.fuelPower/reference.csv new file mode 100644 index 0000000000..dfe35a2d0d --- /dev/null +++ b/docs/issue1147_GenericBoiler/regression/Systems/funnel_comp/AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.mat_boilerControlBus.fuelPower/reference.csv @@ -0,0 +1,102 @@ +x,y +0.000000,54272.542969 +840.000000,29000.427734 +1680.000000,30491.628906 +2520.000000,31591.613281 +3360.000000,32481.611328 +4200.000000,33109.542969 +5040.000000,33438.753906 +5880.000000,33450.015625 +6720.000000,33142.656250 +7560.000000,32534.623047 +8400.000000,31661.423828 +9240.000000,30574.185547 +10080.000000,29336.740234 +10920.000000,28022.072266 +11760.000000,26708.027344 +12600.000000,25472.849609 +13440.000000,24390.437500 +14280.000000,23523.757812 +15120.000000,22927.253906 +15960.000000,22637.847656 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+81479.999070,22670.747735 +82319.999000,22983.788953 +83159.999000,23602.246637 +83999.999000,24487.314414 +84000.001000,24487.314414 diff --git a/docs/issue1147_GenericBoiler/regression/Systems/simulator-dymola.log b/docs/issue1147_GenericBoiler/regression/Systems/simulator-dymola.log new file mode 100644 index 0000000000..eb3f453716 --- /dev/null +++ b/docs/issue1147_GenericBoiler/regression/Systems/simulator-dymola.log @@ -0,0 +1,2508 @@ + = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Examples.Heater"); +Check of AixLib.Systems.ModularAHU.Examples.Heater: +The model has the same number of unknowns and equations: 2546 +The model could not be deduced to be symbolically well-posed. +The model has + 2490+registerModule.hydraulicModule.valve.vol.dynBal.nPorts+registerModule.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +registerModule.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ registerModule.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ registerModule.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ registerModule.hydraulicModule.junc456.dynBal.nPorts+registerModule.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*registerModule.dynamicHX.vol1[1].dynBal.nPorts+2*registerModule.dynamicHX.vol1[2].dynBal.nPorts +registerModule.dynamicHX.vol2[1].dynBal.nPorts+registerModule.dynamicHX.vol2[2].dynBal.nPorts +scalar unknowns and + 2331+(if boundaryWaterSource.use_Xi_in then 1 else (if boundaryWaterSource.use_X_in then 0 else 1))+(if not boundaryWaterSource.use_p_in then 1 else 0)+2* boundaryWaterSource.nPorts+(if not boundaryWaterSource.use_T_in then 1 else 0) +(if boundaryWaterSink.use_Xi_in then 1 else (if boundaryWaterSink.use_X_in then 0 else 1))+(if not boundaryWaterSink.use_p_in then 1 else 0)+2* boundaryWaterSink.nPorts+(if not boundaryWaterSink.use_T_in then 1 else 0)+( if boundaryAirSource.use_Xi_in then 2 else (if boundaryAirSource.use_X_in then 1 else 3))+3*boundaryAirSource.nPorts+(if not boundaryAirSource.use_p_in then 1 else 0)+(if not boundaryAirSource.use_T_in then 1 else 0)+(if boundaryAirSink.use_Xi_in then 2 else (if boundaryAirSink.use_X_in then 1 else 3))+3*boundaryAirSink.nPorts+(if not boundaryAirSink.use_p_in then 1 else 0)+(if not boundaryAirSink.use_T_in then 1 else 0)+(if not registerModule.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts +(if not registerModule.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.junc456.dynBal.nPorts+(if not registerModule.hydraulicModule.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +(if not registerModule.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +5*registerModule.dynamicHX.vol1[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[2].dynBal.nPorts+(if not registerModule.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3 *registerModule.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2546 +Check of AixLib.Systems.ModularAHU.Examples.Heater successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/Heater.mos\",", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Examples.Heater\",", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Examples.Heater\\\");\",", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Examples.Heater.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/Heater.mos"); +simulateModel("AixLib.Systems.ModularAHU.Examples.Heater", tolerance=1e-6, stopTime=3600, resultFile="AixLib.Systems.ModularAHU.Examples.Heater"); +Translation of AixLib.Systems.ModularAHU.Examples.Heater: +The DAE has 2546 scalar unknowns and 2546 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + if (registerModule.dynamicHX.vol1[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (registerModule.dynamicHX.vol1[1].dynBal.initialize_p) then + registerModule.dynamicHX.vol1[1].dynBal.medium.p = registerModule.dynamicHX.vol1[1].dynBal.p_start; + end if; + else + if (registerModule.dynamicHX.vol1[1].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (registerModule.dynamicHX.vol1[1].dynBal.initialize_p) then + der(registerModule.dynamicHX.vol1[1].dynBal.medium.p) = 0; + end if; + end if; + end if; + if (registerModule.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (registerModule.dynamicHX.vol1[2].dynBal.initialize_p) then + registerModule.dynamicHX.vol1[2].dynBal.medium.p = registerModule.dynamicHX.vol1[2].dynBal.p_start; + end if; + else + if (registerModule.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (registerModule.dynamicHX.vol1[2].dynBal.initialize_p) then + der(registerModule.dynamicHX.vol1[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + +The redundancies involve +initial equations: + 0.0 = 0; + 0.0 = 0; + + +Statistics + +Original Model + Number of components: 549 + Variables: 6673 + Constants: 134 (134 scalars) + Parameters: 3181 (3386 scalars) + Unknowns: 3358 (2653 scalars) + Differentiated variables: 122 scalars + Equations: 2479 + Nontrivial: 1925 +Translated Model + Constants: 2408 scalars + Free parameters: 212 scalars + Parameter depending: 1209 scalars + Continuous time states: 70 scalars + Time-varying variables: 592 scalars + Alias variables: 1752 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {18} + Sizes after manipulation of the nonlinear systems: {2} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {4, 179, 12} + Sizes after manipulation of the linear systems: {2, 59, 2} + Sizes of nonlinear systems of equations: {1, 18, 1} + Sizes after manipulation of the nonlinear systems: {0, 3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + ctrBasic.PID.D.x + ctrBasic.PID.I.y + registerModule.dynamicHX.heatCapacitor[1].T + registerModule.dynamicHX.heatCapacitor[2].T + registerModule.dynamicHX.vol1[1].dynBal.medium.T + registerModule.dynamicHX.vol1[1].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[2].dynBal.medium.T + registerModule.dynamicHX.vol1[2].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol2[1].dynBal.medium.T + registerModule.dynamicHX.vol2[2].dynBal.medium.T + registerModule.hydraulicModule.junc456.dynBal.medium.T + registerModule.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.medium.T + registerModule.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.medium.T + registerModule.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.medium.T + registerModule.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.medium.T + registerModule.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.medium.T + registerModule.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.medium.T + registerModule.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.medium.T + registerModule.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.medium.T + registerModule.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.medium.T + registerModule.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.medium.T + registerModule.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.medium.T + registerModule.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.medium.T + registerModule.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.medium.T + registerModule.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.medium.T + registerModule.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.medium.T + registerModule.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.medium.T + registerModule.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.medium.T + registerModule.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.medium.T + registerModule.hydraulicModule.PT1_a1.y + registerModule.hydraulicModule.PT1_a2.y + registerModule.hydraulicModule.PT1_b1.y + registerModule.hydraulicModule.PT1_b2.y + registerModule.hydraulicModule.PumpInterface.pump.filter.s[1] + registerModule.hydraulicModule.PumpInterface.pump.filter.s[2] + registerModule.hydraulicModule.PumpInterface.pump.vol.dynBal.medium.T + registerModule.hydraulicModule.senT_a1.T + registerModule.hydraulicModule.senT_a2.T + registerModule.hydraulicModule.senT_b1.T + registerModule.hydraulicModule.senT_b2.T + registerModule.hydraulicModule.valve.filter.s[1] + registerModule.hydraulicModule.valve.vol.dynBal.medium.T + registerModule.PT1_airIn.y + registerModule.PT1_airOut.y + registerModule.senT_airIn.T + registerModule.senT_airOut.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Examples.Heater.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Injection"); +Check of AixLib.Systems.HydraulicModules.Example.Injection: +The model has the same number of unknowns and equations: 3023 +The model could not be deduced to be symbolically well-posed. +The model has + 2955+Injection.valve.vol.dynBal.nPorts+Injection.pipe1.simplePipe.vol[1].dynBal.nPorts +Injection.pipe1.simplePipe.vol[2].dynBal.nPorts+Injection.pipe1.simplePipe.vol[3].dynBal.nPorts +Injection.pipe2.simplePipe.vol[1].dynBal.nPorts+Injection.pipe2.simplePipe.vol[2].dynBal.nPorts +Injection.pipe2.simplePipe.vol[3].dynBal.nPorts+Injection.pipe3.simplePipe.vol[1].dynBal.nPorts +Injection.pipe3.simplePipe.vol[2].dynBal.nPorts+Injection.pipe3.simplePipe.vol[3].dynBal.nPorts +Injection.pipe4.simplePipe.vol[1].dynBal.nPorts+Injection.pipe4.simplePipe.vol[2].dynBal.nPorts +Injection.pipe4.simplePipe.vol[3].dynBal.nPorts+Injection.pipe5.simplePipe.vol[1].dynBal.nPorts +Injection.pipe5.simplePipe.vol[2].dynBal.nPorts+Injection.pipe5.simplePipe.vol[3].dynBal.nPorts +Injection.pipe6.simplePipe.vol[1].dynBal.nPorts+Injection.pipe6.simplePipe.vol[2].dynBal.nPorts +Injection.pipe6.simplePipe.vol[3].dynBal.nPorts+Injection.pipe7.simplePipe.vol[1].dynBal.nPorts +Injection.pipe7.simplePipe.vol[2].dynBal.nPorts+Injection.pipe7.simplePipe.vol[3].dynBal.nPorts +Injection.pipe8.simplePipe.vol[1].dynBal.nPorts+Injection.pipe8.simplePipe.vol[2].dynBal.nPorts +Injection.pipe8.simplePipe.vol[3].dynBal.nPorts+Injection.pipe9.simplePipe.vol[1].dynBal.nPorts +Injection.pipe9.simplePipe.vol[2].dynBal.nPorts+Injection.pipe9.simplePipe.vol[3].dynBal.nPorts +Injection.junc3v6.dynBal.nPorts+Injection.PumpInterface.pump.vol.dynBal.nPorts +Injection.junc15j.dynBal.nPorts+Injection.juncjp6.dynBal.nPorts +scalar unknowns and + 2777+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Injection.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe3.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe4.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe4.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe4.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe5.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe5.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe5.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe6.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe6.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe6.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe7.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe7.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe7.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe8.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe8.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe8.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe8.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe8.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe8.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe9.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe9.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe9.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe9.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe9.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe9.simplePipe.vol[3].dynBal.nPorts+(if not Injection.junc3v6.dynBal.use_mWat_flow then 1 else 0)+3*Injection.junc3v6.dynBal.nPorts+(if not Injection.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*Injection.PumpInterface.pump.vol.dynBal.nPorts+(if not Injection.junc15j.dynBal.use_mWat_flow then 1 else 0)+3*Injection.junc15j.dynBal.nPorts +(if not Injection.juncjp6.dynBal.use_mWat_flow then 1 else 0)+3* Injection.juncjp6.dynBal.nPorts+(if not Injection.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3*Injection.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 3023 +Check of AixLib.Systems.HydraulicModules.Example.Injection successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Injection.mos\",", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Injection\",", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Injection\\\");\",", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Injection.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Injection.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Injection", tolerance=1e-6, stopTime=800, resultFile="AixLib.Systems.HydraulicModules.Example.Injection"); +Translation of AixLib.Systems.HydraulicModules.Example.Injection: +The DAE has 3023 scalar unknowns and 3023 scalar equations. + +Statistics + +Original Model + Number of components: 665 + Variables: 8147 + Constants: 161 (161 scalars) + Parameters: 3917 (4056 scalars) + Unknowns: 4069 (3142 scalars) + Differentiated variables: 111 scalars + Equations: 2963 + Nontrivial: 2268 +Translated Model + Constants: 2976 scalars + Free parameters: 199 scalars + Parameter depending: 1398 scalars + Outputs: 13 scalars + Continuous time states: 79 scalars + Time-varying variables: 671 scalars + Alias variables: 2115 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {26} + Sizes after manipulation of the nonlinear systems: {3} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {26, 1} + Sizes after manipulation of the nonlinear systems: {4, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + Injection.junc3v6.dynBal.U + Injection.junc15j.dynBal.U + Injection.juncjp6.dynBal.U + Injection.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe1.simplePipe.vol[1].dynBal.U + Injection.pipe1.simplePipe.vol[2].dynBal.U + Injection.pipe1.simplePipe.vol[3].dynBal.U + Injection.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe2.simplePipe.vol[1].dynBal.U + Injection.pipe2.simplePipe.vol[2].dynBal.U + Injection.pipe2.simplePipe.vol[3].dynBal.U + Injection.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe3.simplePipe.vol[1].dynBal.U + Injection.pipe3.simplePipe.vol[2].dynBal.U + Injection.pipe3.simplePipe.vol[3].dynBal.U + Injection.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe4.simplePipe.vol[1].dynBal.U + Injection.pipe4.simplePipe.vol[2].dynBal.U + Injection.pipe4.simplePipe.vol[3].dynBal.U + Injection.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe5.simplePipe.vol[1].dynBal.U + Injection.pipe5.simplePipe.vol[2].dynBal.U + Injection.pipe5.simplePipe.vol[3].dynBal.U + Injection.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe6.simplePipe.vol[1].dynBal.U + Injection.pipe6.simplePipe.vol[2].dynBal.U + Injection.pipe6.simplePipe.vol[3].dynBal.U + Injection.pipe7.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe7.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe7.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe7.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe7.simplePipe.vol[1].dynBal.U + Injection.pipe7.simplePipe.vol[2].dynBal.U + Injection.pipe7.simplePipe.vol[3].dynBal.U + Injection.pipe8.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe8.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe8.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe8.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe8.simplePipe.vol[1].dynBal.U + Injection.pipe8.simplePipe.vol[2].dynBal.U + Injection.pipe8.simplePipe.vol[3].dynBal.U + Injection.pipe9.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe9.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe9.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe9.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe9.simplePipe.vol[1].dynBal.U + Injection.pipe9.simplePipe.vol[2].dynBal.U + Injection.pipe9.simplePipe.vol[3].dynBal.U + Injection.PT1_a1.y + Injection.PT1_a2.y + Injection.PT1_b1.y + Injection.PT1_b2.y + Injection.PumpInterface.pump.filter.s[1] + Injection.PumpInterface.pump.filter.s[2] + Injection.PumpInterface.pump.vol.dynBal.U + Injection.senT_a1.T + Injection.senT_a2.T + Injection.senT_b1.T + Injection.senT_b2.T + Injection.valve.filter.s[1] + Injection.valve.vol.dynBal.U + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Injection.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Pump"); +Check of AixLib.Systems.HydraulicModules.Example.Pump: +The model has the same number of unknowns and equations: 916 +The model could not be deduced to be symbolically well-posed. +The model has + 902+Unmixed.PumpInterface.pump.vol.dynBal.nPorts+Unmixed.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +Unmixed.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+Unmixed.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +Unmixed.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+Unmixed.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +Unmixed.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +scalar unknowns and + 857+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Unmixed.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3* Unmixed.PumpInterface.pump.vol.dynBal.nPorts+(if not Unmixed.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*Unmixed.pipe1.plugFlowPipe.vol_b.dynBal.nPorts+(if not Unmixed.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3* Unmixed.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+(if not Unmixed.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*Unmixed.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+(if not Unmixed.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3* Unmixed.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+(if not Unmixed.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*Unmixed.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+(if not Unmixed.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3* Unmixed.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 916 +Check of AixLib.Systems.HydraulicModules.Example.Pump successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Pump.mos\",", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Pump\",", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Pump\\\");\",", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Pump.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Pump.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Pump", tolerance=1e-6, outputInterval=5, stopTime=800, resultFile="AixLib.Systems.HydraulicModules.Example.Pump"); +Translation of AixLib.Systems.HydraulicModules.Example.Pump: +The DAE has 916 scalar unknowns and 916 scalar equations. + +Statistics + +Original Model + Number of components: 195 + Variables: 2528 + Constants: 42 (42 scalars) + Parameters: 1214 (1411 scalars) + Unknowns: 1272 (954 scalars) + Differentiated variables: 33 scalars + Equations: 1018 + Nontrivial: 814 +Translated Model + Constants: 936 scalars + Free parameters: 127 scalars + Parameter depending: 522 scalars + Outputs: 10 scalars + Continuous time states: 26 scalars + Time-varying variables: 227 scalars + Alias variables: 595 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0} + Sizes of nonlinear systems of equations: {10, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {10, 1} + Sizes after manipulation of the nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + Unmixed.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + Unmixed.pipe1.plugFlowPipe.del.x + Unmixed.pipe1.plugFlowPipe.timDel.x + Unmixed.pipe1.plugFlowPipe.vol_a.dynBal.U + Unmixed.pipe1.plugFlowPipe.vol_b.dynBal.U + Unmixed.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + Unmixed.pipe2.plugFlowPipe.del.x + Unmixed.pipe2.plugFlowPipe.timDel.x + Unmixed.pipe2.plugFlowPipe.vol_a.dynBal.U + Unmixed.pipe2.plugFlowPipe.vol_b.dynBal.U + Unmixed.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + Unmixed.pipe3.plugFlowPipe.del.x + Unmixed.pipe3.plugFlowPipe.timDel.x + Unmixed.pipe3.plugFlowPipe.vol_a.dynBal.U + Unmixed.pipe3.plugFlowPipe.vol_b.dynBal.U + Unmixed.PT1_a1.y + Unmixed.PT1_a2.y + Unmixed.PT1_b1.y + Unmixed.PT1_b2.y + Unmixed.PumpInterface.pump.filter.s[1] + Unmixed.PumpInterface.pump.filter.s[2] + Unmixed.PumpInterface.pump.vol.dynBal.U + Unmixed.senT_a1.T + Unmixed.senT_a2.T + Unmixed.senT_b1.T + Unmixed.senT_b2.T + +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Pump.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple"); +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple: +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.m_flow. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-0-fzh2_uav/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.dp. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-0-fzh2_uav/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +The model has the same number of unknowns and equations: 575 +The model could not be deduced to be symbolically well-posed. +The model has + 545+modularBoiler.boilerGeneric.vol.dynBal.nPorts+2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1 +2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.offDesignOperation.boilerEffciency.nin +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n1+2* modularBoiler.boilerGeneric.designOperation.multiplex4.n2+2*modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.boilerEffciency.nin +modularBoiler.pump.vol.dynBal.nPorts+vol.dynBal.nPorts +scalar unknowns and + 533+2*(modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1+ modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3 +modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.multiplex4.n1 +modularBoiler.boilerGeneric.designOperation.multiplex4.n2+modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +modularBoiler.boilerGeneric.designOperation.multiplex4.n4)+(if bou.use_Xi_in then 1 else (if bou.use_X_in then 0 else 1))+(if not bou.use_p_in then 1 else 0)+2*bou.nPorts+(if not bou.use_T_in then 1 else 0)+(if not modularBoiler.boilerGeneric.vol.dynBal.use_mWat_flow then 1 else 0)+3* modularBoiler.boilerGeneric.vol.dynBal.nPorts+(if not modularBoiler.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*modularBoiler.pump.vol.dynBal.nPorts+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 575 +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple successful. +Warning: WARNINGS have been issued. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerSimple.mos\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple\\\");\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerSimple.mos"); +simulateModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple", tolerance=1e-06, stopTime=84000, method="dassl", resultFile="AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple"); +Translation of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple: +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.m_flow. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-0-fzh2_uav/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.dp. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-0-fzh2_uav/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +The DAE has 575 scalar unknowns and 575 scalar equations. +Warning: The initial conditions are not fully specified. +Dymola has selected default initial conditions. +Warning: Assuming fixed start value for the continuous states: + vol.dynBal.U(start = 4165531.824*(vol.dynBal.fluidVolume*(vol.dynBal.T_start -273.15))) + + +Statistics + +Original Model + Number of components: 156 + Variables: 1280 + Constants: 18 (18 scalars) + Parameters: 621 (745 scalars) + Unknowns: 641 (594 scalars) + Differentiated variables: 14 scalars + Equations: 586 + Nontrivial: 485 +Translated Model + Constants: 412 scalars + Free parameters: 127 scalars + Parameter depending: 293 scalars + Outputs: 10 scalars + Continuous time states: 10 scalars + Time-varying variables: 143 scalars + Alias variables: 382 scalars + Assumed default initial conditions: 1 + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: {5} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {5} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + modularBoiler.boilerControl.internalFirRatControl.PID.I.y + modularBoiler.boilerGeneric.senTRet.T + modularBoiler.boilerGeneric.senTSup.T + modularBoiler.boilerGeneric.vol.dynBal.U + modularBoiler.pump.filter.s[1] + modularBoiler.pump.filter.s[2] + modularBoiler.pump.vol.dynBal.U + modularBoiler.senTRet.T + modularBoiler.senTSup.T + vol.dynBal.U + +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerSimple.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve"); +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve: +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.m_flow. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-1-fbxcmbpp/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.dp. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-1-fbxcmbpp/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +The model has the same number of unknowns and equations: 604 +The model could not be deduced to be symbolically well-posed. +The model has + 574+modularBoiler.boilerGeneric.vol.dynBal.nPorts+2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1 +2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.offDesignOperation.boilerEffciency.nin +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n1+2* modularBoiler.boilerGeneric.designOperation.multiplex4.n2+2*modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.boilerEffciency.nin +modularBoiler.pump.vol.dynBal.nPorts+vol.dynBal.nPorts +scalar unknowns and + 562+2*(modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1+ modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3 +modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.multiplex4.n1 +modularBoiler.boilerGeneric.designOperation.multiplex4.n2+modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +modularBoiler.boilerGeneric.designOperation.multiplex4.n4)+(if bou.use_Xi_in then 1 else (if bou.use_X_in then 0 else 1))+(if not bou.use_p_in then 1 else 0)+2*bou.nPorts+(if not bou.use_T_in then 1 else 0)+(if not modularBoiler.boilerGeneric.vol.dynBal.use_mWat_flow then 1 else 0)+3* modularBoiler.boilerGeneric.vol.dynBal.nPorts+(if not modularBoiler.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*modularBoiler.pump.vol.dynBal.nPorts+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 604 +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve successful. +Warning: WARNINGS have been issued. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerHeatingCurve.mos\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve\\\");\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerHeatingCurve.mos"); +simulateModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve", tolerance=1e-06, stopTime=84000, method="dassl", resultFile="AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve"); +Translation of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve: +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.m_flow. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-1-fbxcmbpp/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.dp. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-1-fbxcmbpp/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +The DAE has 604 scalar unknowns and 604 scalar equations. +Warning: The initial conditions are not fully specified. +Dymola has selected default initial conditions. +Warning: Assuming fixed start value for the continuous states: + vol.dynBal.U(start = 4165531.824*(vol.dynBal.fluidVolume*(vol.dynBal.T_start -273.15))) + + +Statistics + +Original Model + Number of components: 167 + Variables: 1369 + Constants: 26 (118 scalars) + Parameters: 668 (1192 scalars) + Unknowns: 675 (623 scalars) + Differentiated variables: 14 scalars + Equations: 606 + Nontrivial: 504 +Translated Model + Constants: 536 scalars + Free parameters: 328 scalars + Parameter depending: 516 scalars + Outputs: 9 scalars + Continuous time states: 10 scalars + Time-varying variables: 163 scalars + Alias variables: 390 scalars + Assumed default initial conditions: 1 + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: {5} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {5} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + modularBoiler.boilerControl.internalFirRatControl.PID.I.y + modularBoiler.boilerGeneric.senTRet.T + modularBoiler.boilerGeneric.senTSup.T + modularBoiler.boilerGeneric.vol.dynBal.U + modularBoiler.pump.filter.s[1] + modularBoiler.pump.filter.s[2] + modularBoiler.pump.vol.dynBal.U + modularBoiler.senTRet.T + modularBoiler.senTSup.T + vol.dynBal.U + +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerHeatingCurve.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Validation.AHU2_Cooler"); +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Cooler: +The model has the same number of unknowns and equations: 2420 +The model could not be deduced to be symbolically well-posed. +The model has + 2341+max([size(combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+ registerModule.hydraulicModule.valve.vol.dynBal.nPorts+registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.junc456.dynBal.nPorts+2*size(registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+2*registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+ registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+2* registerModule.dynamicHX.vol1[1].dynBal.nPorts+2*registerModule.dynamicHX.vol1[2].dynBal.nPorts +2*registerModule.dynamicHX.vol1[3].dynBal.nPorts+2*registerModule.dynamicHX.vol1[4].dynBal.nPorts +registerModule.dynamicHX.vol2[1].dynBal.nPorts+registerModule.dynamicHX.vol2[2].dynBal.nPorts +registerModule.dynamicHX.vol2[3].dynBal.nPorts+registerModule.dynamicHX.vol2[4].dynBal.nPorts +scalar unknowns and + 2193+(if boundaryWaterSource.use_Xi_in then 1 else (if boundaryWaterSource.use_X_in then 0 else 1))+(if not boundaryWaterSource.use_p_in then 1 else 0)+2* boundaryWaterSource.nPorts+(if not boundaryWaterSource.use_T_in then 1 else 0) +(if boundaryWaterSink.use_Xi_in then 1 else (if boundaryWaterSink.use_X_in then 0 else 1))+(if not boundaryWaterSink.use_p_in then 1 else 0)+2* boundaryWaterSink.nPorts+(if not boundaryWaterSink.use_T_in then 1 else 0)+( if boundaryAirSource.use_Xi_in then 2 else (if boundaryAirSource.use_X_in then 1 else 3))+3*boundaryAirSource.nPorts+(if not boundaryAirSource.use_m_flow_in then 1 else 0)+(if not boundaryAirSource.use_T_in then 1 else 0)+(if boundaryAirSink.use_Xi_in then 2 else (if boundaryAirSink.use_X_in then 1 else 3))+3*boundaryAirSink.nPorts+(if not boundaryAirSink.use_p_in then 1 else 0)+(if not boundaryAirSink.use_T_in then 1 else 0)+max([size( combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+2*size( registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.junc456.dynBal.nPorts+(if not registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +(if not registerModule.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +5*registerModule.dynamicHX.vol1[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+5* registerModule.dynamicHX.vol1[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[4].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[4].dynBal.nPorts+(if not registerModule.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3 *registerModule.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2420 +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Cooler successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Cooler.mos\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Validation.AHU2_Cooler\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Validation.AHU2_Cooler\\\");\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Cooler.mos"); +simulateModel("AixLib.Systems.ModularAHU.Validation.AHU2_Cooler", tolerance=1e-6, outputInterval=1, stopTime=2700, resultFile="AixLib.Systems.ModularAHU.Validation.AHU2_Cooler"); +Translation of AixLib.Systems.ModularAHU.Validation.AHU2_Cooler: +The DAE has 2420 scalar unknowns and 2420 scalar equations. + +Statistics + +Original Model + Number of components: 464 + Variables: 6155 + Constants: 125 (125 scalars) + Parameters: 2790 (41180 scalars) + Unknowns: 3240 (2523 scalars) + Differentiated variables: 86 scalars + Equations: 2514 + Nontrivial: 1950 +Translated Model + Constants: 2376 scalars + Free parameters: 19299 scalars + Parameter depending: 19948 scalars + Outputs: 17 scalars + Continuous time states: 62 scalars + Time-varying variables: 629 scalars + Alias variables: 1576 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {17, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {2, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {17, 1} + Sizes after manipulation of the nonlinear systems: {3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + registerModule.dynamicHX.heatCapacitor[1].T + registerModule.dynamicHX.heatCapacitor[2].T + registerModule.dynamicHX.heatCapacitor[3].T + registerModule.dynamicHX.heatCapacitor[4].T + registerModule.dynamicHX.vol1[1].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[1].dynBal.U + registerModule.dynamicHX.vol1[2].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[2].dynBal.U + registerModule.dynamicHX.vol1[3].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[3].dynBal.U + registerModule.dynamicHX.vol1[4].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[4].dynBal.U + registerModule.dynamicHX.vol2[1].dynBal.U + registerModule.dynamicHX.vol2[2].dynBal.U + registerModule.dynamicHX.vol2[3].dynBal.U + registerModule.dynamicHX.vol2[4].dynBal.U + registerModule.hydraulicModule.junc456.dynBal.U + registerModule.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe1.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe1.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe2.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe2.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe3.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe3.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe4.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe4.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe5.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe5.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe6.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe6.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.PT1_a1.y + registerModule.hydraulicModule.PT1_a2.y + registerModule.hydraulicModule.PT1_b1.y + registerModule.hydraulicModule.PT1_b2.y + registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] + registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] + registerModule.hydraulicModule.senT_a1.T + registerModule.hydraulicModule.senT_a2.T + registerModule.hydraulicModule.senT_b1.T + registerModule.hydraulicModule.senT_b2.T + registerModule.hydraulicModule.valve.vol.dynBal.U + registerModule.PT1_airIn.y + registerModule.PT1_airOut.y + registerModule.senT_airIn.T + registerModule.senT_airOut.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Validation.AHU2_Cooler.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Examples.DemandControlledAHU"); +Check of AixLib.Systems.ModularAHU.Examples.DemandControlledAHU: +The model has the same number of unknowns and equations: 11521 +The model could not be deduced to be symbolically well-posed. +The model has + 11048+genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+2*size( genericAHU.preheater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+2*genericAHU.preheater.hydraulicModule.PumpInterface.physics.deMultiplex2.n1 +2*genericAHU.preheater.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.preheater.hydraulicModule.PumpInterface.physics.criticalDamping.n+ genericAHU.preheater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+3 *genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts +3*genericAHU.preheater.dynamicHX.vol1[3].dynBal.nPorts+3*genericAHU.preheater.dynamicHX.vol1[4].dynBal.nPorts +3*genericAHU.preheater.dynamicHX.vol1[5].dynBal.nPorts+genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts +genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+genericAHU.preheater.dynamicHX.vol2[3].dynBal.nPorts +genericAHU.preheater.dynamicHX.vol2[4].dynBal.nPorts+genericAHU.preheater.dynamicHX.vol2[5].dynBal.nPorts +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts+genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+2*size( genericAHU.cooler.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1) +2*genericAHU.cooler.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* genericAHU.cooler.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.cooler.hydraulicModule.PumpInterface.physics.criticalDamping.n+ genericAHU.cooler.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+3* genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts +3*genericAHU.cooler.dynamicHX.vol1[3].dynBal.nPorts+3*genericAHU.cooler.dynamicHX.vol1[4].dynBal.nPorts +genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts +genericAHU.cooler.dynamicHX.vol2[3].dynBal.nPorts+genericAHU.cooler.dynamicHX.vol2[4].dynBal.nPorts +genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+2*size( genericAHU.heater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1) +2*genericAHU.heater.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* genericAHU.heater.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.heater.hydraulicModule.PumpInterface.physics.criticalDamping.n+ genericAHU.heater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+3* genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts +3*genericAHU.heater.dynamicHX.vol1[3].dynBal.nPorts+3*genericAHU.heater.dynamicHX.vol1[4].dynBal.nPorts +genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts +genericAHU.heater.dynamicHX.vol2[3].dynBal.nPorts+genericAHU.heater.dynamicHX.vol2[4].dynBal.nPorts +3*genericAHU.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.dynamicHX.vol1[2].dynBal.nPorts +3*genericAHU.dynamicHX.vol2[1].dynBal.nPorts+3*genericAHU.dynamicHX.vol2[2].dynBal.nPorts +3*genericAHU.fanSup.vol.dynBal.nPorts+3*genericAHU.fanRet.vol.dynBal.nPorts+3 *genericAHU.humidifier.vol.dynBal.nPorts+29*thermalZone.zoneParam.nOrientations +3*thermalZone.ROM.volMoiAir.dynBal.nPorts+thermalZone.humanTotHeaDependent.productHeatOutput.nu +thermalZone.humanTotHeaDependent.productMoistureOutput.nu+thermalZone.machinesSenHea.productHeatOutput.nu +thermalZone.lights.productHeatOutput.nu+thermalZone.ventCont.optimalTemp.nin+ thermalZone.ventCont.optimalTemp.nout+thermalZone.ventCont.dEMA.nout+ thermalZone.ventCont.dEMA.ExpAVG.n+thermalZone.ventCont.dEMA.ExpAVG1.n+ thermalZone.SumQLat2_flow.nu+max([size(internalGains.columns, 1); size( internalGains.offset, 1)]) +scalar unknowns and + 10574+size(genericAHU.preheater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+genericAHU.preheater.hydraulicModule.PumpInterface.physics.deMultiplex2.n1 +genericAHU.preheater.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.preheater.hydraulicModule.PumpInterface.physics.criticalDamping.n-1 +size(genericAHU.cooler.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+genericAHU.cooler.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ genericAHU.cooler.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.cooler.hydraulicModule.PumpInterface.physics.criticalDamping.n-1+ size(genericAHU.heater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+genericAHU.heater.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ genericAHU.heater.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ genericAHU.heater.hydraulicModule.PumpInterface.physics.criticalDamping.n-1+( if not genericAHU.humidifier.steamHumidifier then 1 else 0)+(if SourcePreheater.use_Xi_in then 1 else (if SourcePreheater.use_X_in then 0 else 1))+(if not SourcePreheater.use_p_in then 1 else 0)+SourcePreheater.nPorts +(if not SourcePreheater.use_T_in then 1 else 0)+SourcePreheater.nPorts+(if SinkPreheater.use_Xi_in then 1 else (if SinkPreheater.use_X_in then 0 else 1)) +(if not SinkPreheater.use_p_in then 1 else 0)+SinkPreheater.nPorts+(if not SinkPreheater.use_T_in then 1 else 0)+SinkPreheater.nPorts+(if SourceCooler.use_Xi_in then 1 else (if SourceCooler.use_X_in then 0 else 1))+( if not SourceCooler.use_p_in then 1 else 0)+SourceCooler.nPorts+(if not SourceCooler.use_T_in then 1 else 0)+SourceCooler.nPorts+(if SinkCooler.use_Xi_in then 1 else (if SinkCooler.use_X_in then 0 else 1))+(if not SinkCooler.use_p_in then 1 else 0)+SinkCooler.nPorts+(if not SinkCooler.use_T_in then 1 else 0)+ SinkCooler.nPorts+(if SourceHeater.use_Xi_in then 1 else (if SourceHeater.use_X_in then 0 else 1))+(if not SourceHeater.use_p_in then 1 else 0)+ SourceHeater.nPorts+(if not SourceHeater.use_T_in then 1 else 0)+ SourceHeater.nPorts+(if SinkHeater.use_Xi_in then 1 else (if SinkHeater.use_X_in then 0 else 1))+(if not SinkHeater.use_p_in then 1 else 0)+SinkHeater.nPorts +(if not SinkHeater.use_T_in then 1 else 0)+SinkHeater.nPorts+(if not out.x_pTphi.use_p_in then 1 else 0)+(if not out.use_C_in then 1 else 0)+3* out.nPorts+(if boundaryExhaustAir.use_Xi_in then 2 else (if boundaryExhaustAir.use_X_in then 1 else 3))+(if not boundaryExhaustAir.use_C_in then 1 else 0)+2* boundaryExhaustAir.nPorts+(if not boundaryExhaustAir.use_p_in then 1 else 0)+ boundaryExhaustAir.nPorts+(if not boundaryExhaustAir.use_T_in then 1 else 0)+ boundaryExhaustAir.nPorts+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+max([size(internalGains.columns, 1); size (internalGains.offset, 1)])+(if not genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.preheater.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +(if not genericAHU.preheater.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.preheater.dynamicHX.vol1[1].dynBal.use_C_flow then 1 else 0)+3*genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.preheater.dynamicHX.vol1[2].dynBal.use_C_flow then 1 else 0)+3*genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.preheater.dynamicHX.vol1[3].dynBal.use_C_flow then 1 else 0)+3*genericAHU.preheater.dynamicHX.vol1[3].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[3].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.preheater.dynamicHX.vol1[4].dynBal.use_C_flow then 1 else 0)+3*genericAHU.preheater.dynamicHX.vol1[4].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[4].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[5].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.preheater.dynamicHX.vol1[5].dynBal.use_C_flow then 1 else 0)+3*genericAHU.preheater.dynamicHX.vol1[5].dynBal.nPorts+4* genericAHU.preheater.dynamicHX.vol1[5].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[3].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[3].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[4].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[4].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[5].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[5].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[5].dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+( if not genericAHU.cooler.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +(if not genericAHU.cooler.dynamicHX.vol1[1].dynBal.use_C_flow then 1 else 0) +3*genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts+4*genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.cooler.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.cooler.dynamicHX.vol1[2].dynBal.use_C_flow then 1 else 0)+3*genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts+4* genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.cooler.dynamicHX.vol1[3].dynBal.use_C_flow then 1 else 0)+3*genericAHU.cooler.dynamicHX.vol1[3].dynBal.nPorts+4* genericAHU.cooler.dynamicHX.vol1[3].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.cooler.dynamicHX.vol1[4].dynBal.use_C_flow then 1 else 0)+3*genericAHU.cooler.dynamicHX.vol1[4].dynBal.nPorts+4* genericAHU.cooler.dynamicHX.vol1[4].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[3].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[3].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[4].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[4].dynBal.nPorts+(if not genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.heater.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+( if not genericAHU.heater.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +(if not genericAHU.heater.dynamicHX.vol1[1].dynBal.use_C_flow then 1 else 0) +3*genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts+4*genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.heater.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.heater.dynamicHX.vol1[2].dynBal.use_C_flow then 1 else 0)+3*genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts+4* genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.heater.dynamicHX.vol1[3].dynBal.use_C_flow then 1 else 0)+3*genericAHU.heater.dynamicHX.vol1[3].dynBal.nPorts+4* genericAHU.heater.dynamicHX.vol1[3].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.heater.dynamicHX.vol1[4].dynBal.use_C_flow then 1 else 0)+3*genericAHU.heater.dynamicHX.vol1[4].dynBal.nPorts+4* genericAHU.heater.dynamicHX.vol1[4].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[3].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[3].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[4].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[4].dynBal.nPorts+(if not genericAHU.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.dynamicHX.vol1[1].dynBal.use_C_flow then 1 else 0)+3*genericAHU.dynamicHX.vol1[1].dynBal.nPorts+4*genericAHU.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+( if not genericAHU.dynamicHX.vol1[2].dynBal.use_C_flow then 1 else 0)+3* genericAHU.dynamicHX.vol1[2].dynBal.nPorts+4*genericAHU.dynamicHX.vol1[2].dynBal.nPorts +(if not genericAHU.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+( if not genericAHU.dynamicHX.vol2[1].use_C_flow then 1 else 0)+3* genericAHU.dynamicHX.vol2[1].dynBal.nPorts+4*genericAHU.dynamicHX.vol2[1].dynBal.nPorts +(if not genericAHU.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+( if not genericAHU.dynamicHX.vol2[2].use_C_flow then 1 else 0)+3* genericAHU.dynamicHX.vol2[2].dynBal.nPorts+4*genericAHU.dynamicHX.vol2[2].dynBal.nPorts +(if not genericAHU.fanSup.vol.dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.fanSup.vol.use_C_flow then 1 else 0)+3*genericAHU.fanSup.vol.dynBal.nPorts +4*genericAHU.fanSup.vol.dynBal.nPorts+(if not genericAHU.fanRet.vol.dynBal.use_mWat_flow then 1 else 0)+(if not genericAHU.fanRet.vol.use_C_flow then 1 else 0)+3* genericAHU.fanRet.vol.dynBal.nPorts+4*genericAHU.fanRet.vol.dynBal.nPorts+(if not genericAHU.humidifier.vol.use_C_flow then 1 else 0)+3*genericAHU.humidifier.vol.dynBal.nPorts +4*genericAHU.humidifier.vol.dynBal.nPorts+14*thermalZone.zoneParam.nOrientations +(if not thermalZone.eqAirTempWall.TGroundFromInput then 1 else 0)+ thermalZone.zoneParam.nOrientations+2*thermalZone.zoneParam.nOrientations+ thermalZone.ventCont.optimalTemp.nout+thermalZone.ventCont.dEMA.ExpAVG.n-1+ thermalZone.ventCont.dEMA.ExpAVG1.n-1+(if not thermalZone.x_pTphi.use_p_in then 1 else 0)+(if not genericAHU.preheater.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+2 *genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0) +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts+2*genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts +(if not genericAHU.heater.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+2* genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+(if not thermalZone.use_C_flow then 1 else 0)+3*thermalZone.ROM.volMoiAir.dynBal.nPorts +4*thermalZone.ROM.volMoiAir.dynBal.nPorts+size(genericAHU.cooler.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+size(genericAHU.heater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+size(genericAHU.preheater.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+thermalZone.zoneParam.nOrientations+thermalZone.zoneParam.nOrientations +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 11521 +Check of AixLib.Systems.ModularAHU.Examples.DemandControlledAHU successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/DemandControlledAHU.mos\",", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Examples.DemandControlledAHU\",", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Examples.DemandControlledAHU\\\");\",", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/DemandControlledAHU.mos"); +simulateModel("AixLib.Systems.ModularAHU.Examples.DemandControlledAHU", tolerance=1e-5, startTime=5961600, stopTime=6566400, outputInterval=120, resultFile="AixLib.Systems.ModularAHU.Examples.DemandControlledAHU"); +Translation of AixLib.Systems.ModularAHU.Examples.DemandControlledAHU: +The DAE has 11521 scalar unknowns and 11521 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + genericAHU.preheater.dynamicHX.vol1[2].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.preheater.dynamicHX.vol1[3].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.preheater.dynamicHX.vol1[4].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.preheater.dynamicHX.vol1[5].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.cooler.dynamicHX.vol1[2].p_start = genericAHU.cooler.dynamicHX.p1_start; + genericAHU.cooler.dynamicHX.vol1[3].p_start = genericAHU.cooler.dynamicHX.p1_start; + genericAHU.cooler.dynamicHX.vol1[4].p_start = genericAHU.cooler.dynamicHX.p1_start; + genericAHU.heater.dynamicHX.vol1[2].p_start = genericAHU.heater.dynamicHX.p1_start; + genericAHU.heater.dynamicHX.vol1[3].p_start = genericAHU.heater.dynamicHX.p1_start; + genericAHU.heater.dynamicHX.vol1[4].p_start = genericAHU.heater.dynamicHX.p1_start; + genericAHU.dynamicHX.vol1[1].p_start = genericAHU.dynamicHX.p1_start; + genericAHU.dynamicHX.vol2[1].p_start = genericAHU.dynamicHX.p2_start; + genericAHU.fanSup.filter.y_start = genericAHU.fanSup.dp_start; + genericAHU.humidifier.vol.p_start = genericAHU.humidifier.p_start; + if (genericAHU.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (genericAHU.dynamicHX.vol1[2].dynBal.initialize_p) then + genericAHU.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.dynamicHX.vol1[2].dynBal.p_start; + end if; + else + if (genericAHU.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (genericAHU.dynamicHX.vol1[2].dynBal.initialize_p) then + der(genericAHU.dynamicHX.vol1[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + boundaryExhaustAir.p(start = 101325) + genericAHU.dynamicHX.p1_start(start = 101325) + genericAHU.fanSup.dp_start(start = 0) + genericAHU.fanSup.p_start(start = 101325) + genericAHU.humidifier.p_start(start = 101325) + thermalZone.p_start(start = 101325) + +The redundancies involve +initial equations: + genericAHU.fanSup.filter.y = genericAHU.fanSup.filter.y_start; + genericAHU.dampHX.port_a.p = genericAHU.preheater.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.dampHX.port_a.p = genericAHU.preheater.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.dampHX.port_a.p = genericAHU.preheater.dynamicHX.vol1[3].dynBal.p_start; + genericAHU.dampHX.port_a.p = genericAHU.preheater.dynamicHX.vol1[4].dynBal.p_start; + genericAHU.dampHX.port_a.p = genericAHU.preheater.dynamicHX.vol1[5].dynBal.p_start; + genericAHU.cooler.port_b1.p = genericAHU.cooler.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.cooler.port_b1.p = genericAHU.cooler.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.cooler.port_b1.p = genericAHU.cooler.dynamicHX.vol1[3].dynBal.p_start; + genericAHU.cooler.port_b1.p = genericAHU.cooler.dynamicHX.vol1[4].dynBal.p_start; + genericAHU.heater.port_b1.p = genericAHU.heater.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.heater.port_b1.p = genericAHU.heater.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.heater.port_b1.p = genericAHU.heater.dynamicHX.vol1[3].dynBal.p_start; + genericAHU.heater.port_b1.p = genericAHU.heater.dynamicHX.vol1[4].dynBal.p_start; + boundaryExhaustAir.p = genericAHU.dynamicHX.vol1[1].dynBal.p_start; + boundaryExhaustAir.p = genericAHU.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.cooler.port_a1.p = genericAHU.dynamicHX.vol2[1].dynBal.p_start; + genericAHU.cooler.port_a1.p = genericAHU.dynamicHX.vol2[2].dynBal.p_start; + genericAHU.fanSup.port_a.p = genericAHU.fanSup.vol.dynBal.p_start; + genericAHU.fanSup.port_a.p = genericAHU.humidifier.vol.dynBal.p_start; + genericAHU.port_b1.p = thermalZone.ROM.volMoiAir.dynBal.p_start; + +Sparse solver handling possible: false. +Due to flag Advanced.SparseActivate=false. +Model sparse and large enough: true. +Sparse solvers are available for dassl, lsodar, cvode, radau, esdirk*, sdirk* (using OpenMP, set number of cores with Advanced.NumberOfCores). + +Statistics + +Original Model + Number of components: 2017 + Variables: 24959 + Constants: 542 (542 scalars) + Parameters: 10793 (14586 scalars) + Unknowns: 13624 (12024 scalars) + Differentiated variables: 348 scalars + Equations: 10333 + Nontrivial: 8299 +Translated Model + Constants: 8858 scalars + Free parameters: 3360 scalars + Parameter depending: 4150 scalars + Outputs: 23 scalars + Continuous time states: 272 scalars + Time-varying variables: 3262 scalars + Alias variables: 7522 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {6, 5, 3, 5, 5, 22, 4, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 4, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {1, 3, 4, 1, 1, 1, 1, 1, 16, 6, 6, 6, 6, 6, 6, 16, 6, 6, 6, 6, 6, 6, 17, 6, 6, 6, 6, 6, 6, 1, 1, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {0, 1, 1, 0, 0, 0, 0, 0, 2, 1, 1, 1, 1, 1, 1, 2, 1, 1, 1, 1, 1, 1, 2, 1, 1, 1, 1, 1, 1, 0, 1, 0, 1, 0, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {24, 5} + Sizes after manipulation of the linear systems: {4, 0} + Sizes of nonlinear systems of equations: {16, 1, 16, 1, 17, 1, 1, 3, 1, 4, 1, 1, 1, 1} + Sizes after manipulation of the nonlinear systems: {4, 0, 4, 0, 3, 0, 0, 1, 0, 1, 0, 0, 0, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + ctrAHUCO2.ctrCo.PID.D.x + ctrAHUCO2.ctrCo.PID.I.y + ctrAHUCO2.ctrPh.PID.D.x + ctrAHUCO2.ctrPh.PID.I.y + ctrAHUCO2.ctrRh.PID.D.x + ctrAHUCO2.ctrRh.PID.I.y + ctrAHUCO2.PID_CO2.I.y + ctrAHUCO2.PID_SteamHum.I.y + ctrAHUCO2.PID_VflowSup.I.y + genericAHU.cooler.dynamicHX.heatCapacitor[1].T + genericAHU.cooler.dynamicHX.heatCapacitor[2].T + genericAHU.cooler.dynamicHX.heatCapacitor[3].T + genericAHU.cooler.dynamicHX.heatCapacitor[4].T + genericAHU.cooler.dynamicHX.vol1[1].dynBal.mC[1] + genericAHU.cooler.dynamicHX.vol1[1].dynBal.medium.Xi[1] + genericAHU.cooler.dynamicHX.vol1[1].dynBal.U + genericAHU.cooler.dynamicHX.vol1[2].dynBal.mC[1] + genericAHU.cooler.dynamicHX.vol1[2].dynBal.medium.Xi[1] + genericAHU.cooler.dynamicHX.vol1[2].dynBal.U + genericAHU.cooler.dynamicHX.vol1[3].dynBal.mC[1] + genericAHU.cooler.dynamicHX.vol1[3].dynBal.medium.Xi[1] + genericAHU.cooler.dynamicHX.vol1[3].dynBal.U + genericAHU.cooler.dynamicHX.vol1[4].dynBal.mC[1] + genericAHU.cooler.dynamicHX.vol1[4].dynBal.medium.Xi[1] + genericAHU.cooler.dynamicHX.vol1[4].dynBal.U + genericAHU.cooler.dynamicHX.vol2[1].dynBal.U + genericAHU.cooler.dynamicHX.vol2[2].dynBal.U + genericAHU.cooler.dynamicHX.vol2[3].dynBal.U + genericAHU.cooler.dynamicHX.vol2[4].dynBal.U + genericAHU.cooler.hydraulicModule.junc456.dynBal.U + genericAHU.cooler.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.del.x + genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.timDel.x + genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U + genericAHU.cooler.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U + genericAHU.cooler.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.del.x + genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.timDel.x + genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U + genericAHU.cooler.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U + genericAHU.cooler.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.del.x + genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.timDel.x + genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U + genericAHU.cooler.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U + genericAHU.cooler.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.del.x + genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.timDel.x + genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U + genericAHU.cooler.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U + genericAHU.cooler.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.del.x + genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.timDel.x + genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U + genericAHU.cooler.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U + genericAHU.cooler.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.del.x + genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.timDel.x + genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U + genericAHU.cooler.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U + genericAHU.cooler.hydraulicModule.PT1_a1.y + genericAHU.cooler.hydraulicModule.PT1_a2.y + genericAHU.cooler.hydraulicModule.PT1_b1.y + genericAHU.cooler.hydraulicModule.PT1_b2.y + genericAHU.cooler.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] + genericAHU.cooler.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] + genericAHU.cooler.hydraulicModule.senT_a1.T + genericAHU.cooler.hydraulicModule.senT_a2.T + genericAHU.cooler.hydraulicModule.senT_b1.T + genericAHU.cooler.hydraulicModule.senT_b2.T + genericAHU.cooler.hydraulicModule.valve.filter.s[1] + genericAHU.cooler.hydraulicModule.valve.vol.dynBal.U + genericAHU.cooler.port_a1.p + genericAHU.cooler.port_b1.p + genericAHU.cooler.PT1_airIn.y + genericAHU.cooler.PT1_airOut.y + genericAHU.cooler.senT_airIn.T + genericAHU.cooler.senT_airOut.T + genericAHU.dampBypass.filter.s[1] + genericAHU.dampBypass.filter.s[2] + genericAHU.dampHX.filter.s[1] + genericAHU.dampHX.filter.s[2] + genericAHU.dampHX.port_a.p + genericAHU.dynamicHX.heatCapacitor[1].T + genericAHU.dynamicHX.heatCapacitor[2].T + genericAHU.dynamicHX.vol1[1].dynBal.mC[1] + genericAHU.dynamicHX.vol1[1].dynBal.medium.Xi[1] + genericAHU.dynamicHX.vol1[1].dynBal.U + genericAHU.dynamicHX.vol1[2].dynBal.mC[1] + genericAHU.dynamicHX.vol1[2].dynBal.medium.Xi[1] + genericAHU.dynamicHX.vol1[2].dynBal.U + genericAHU.dynamicHX.vol2[1].dynBal.mC[1] + genericAHU.dynamicHX.vol2[1].dynBal.medium.Xi[1] + genericAHU.dynamicHX.vol2[1].dynBal.U + genericAHU.dynamicHX.vol2[2].dynBal.mC[1] + genericAHU.dynamicHX.vol2[2].dynBal.medium.Xi[1] + genericAHU.dynamicHX.vol2[2].dynBal.U + genericAHU.fanRet.filter.s[1] + genericAHU.fanRet.filter.s[2] + genericAHU.fanRet.vol.dynBal.m + genericAHU.fanRet.vol.dynBal.mC[1] + genericAHU.fanRet.vol.dynBal.medium.Xi[1] + genericAHU.fanRet.vol.dynBal.U + genericAHU.fanSup.filter.s[1] + genericAHU.fanSup.filter.s[2] + genericAHU.fanSup.vol.dynBal.mC[1] + genericAHU.fanSup.vol.dynBal.medium.Xi[1] + genericAHU.fanSup.vol.dynBal.U + genericAHU.flapRet.filter.s[1] + genericAHU.flapRet.filter.s[2] + genericAHU.flapSup.filter.s[1] + genericAHU.flapSup.filter.s[2] + genericAHU.heater.dynamicHX.heatCapacitor[1].T + genericAHU.heater.dynamicHX.heatCapacitor[2].T + genericAHU.heater.dynamicHX.heatCapacitor[3].T + genericAHU.heater.dynamicHX.heatCapacitor[4].T + genericAHU.heater.dynamicHX.vol1[1].dynBal.mC[1] + genericAHU.heater.dynamicHX.vol1[1].dynBal.medium.Xi[1] + genericAHU.heater.dynamicHX.vol1[1].dynBal.U + genericAHU.heater.dynamicHX.vol1[2].dynBal.mC[1] + genericAHU.heater.dynamicHX.vol1[2].dynBal.medium.Xi[1] + genericAHU.heater.dynamicHX.vol1[2].dynBal.U + genericAHU.heater.dynamicHX.vol1[3].dynBal.mC[1] + genericAHU.heater.dynamicHX.vol1[3].dynBal.medium.Xi[1] + genericAHU.heater.dynamicHX.vol1[3].dynBal.U + genericAHU.heater.dynamicHX.vol1[4].dynBal.mC[1] + genericAHU.heater.dynamicHX.vol1[4].dynBal.medium.Xi[1] + genericAHU.heater.dynamicHX.vol1[4].dynBal.U + genericAHU.heater.dynamicHX.vol2[1].dynBal.U + genericAHU.heater.dynamicHX.vol2[2].dynBal.U + genericAHU.heater.dynamicHX.vol2[3].dynBal.U + genericAHU.heater.dynamicHX.vol2[4].dynBal.U + genericAHU.heater.hydraulicModule.junc456.dynBal.U + genericAHU.heater.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.del.x + genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.timDel.x + genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U + genericAHU.heater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U + genericAHU.heater.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.del.x + genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.timDel.x + genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U + genericAHU.heater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U + genericAHU.heater.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.del.x + genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.timDel.x + genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U + genericAHU.heater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U + genericAHU.heater.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.del.x + genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.timDel.x + genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U + genericAHU.heater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U + genericAHU.heater.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.del.x + genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.timDel.x + genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U + genericAHU.heater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U + genericAHU.heater.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.del.x + genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.timDel.x + genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U + genericAHU.heater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U + genericAHU.heater.hydraulicModule.PT1_a1.y + genericAHU.heater.hydraulicModule.PT1_a2.y + genericAHU.heater.hydraulicModule.PT1_b1.y + genericAHU.heater.hydraulicModule.PT1_b2.y + genericAHU.heater.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] + genericAHU.heater.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] + genericAHU.heater.hydraulicModule.senT_a1.T + genericAHU.heater.hydraulicModule.senT_a2.T + genericAHU.heater.hydraulicModule.senT_b1.T + genericAHU.heater.hydraulicModule.senT_b2.T + genericAHU.heater.hydraulicModule.valve.vol.dynBal.U + genericAHU.heater.port_b1.p + genericAHU.heater.PT1_airIn.y + genericAHU.heater.PT1_airOut.y + genericAHU.heater.senT_airIn.T + genericAHU.heater.senT_airOut.T + genericAHU.humidifier.vol.dynBal.mC[1] + genericAHU.humidifier.vol.dynBal.medium.Xi[1] + genericAHU.humidifier.vol.dynBal.U + genericAHU.preheater.dynamicHX.heatCapacitor[1].T + genericAHU.preheater.dynamicHX.heatCapacitor[2].T + genericAHU.preheater.dynamicHX.heatCapacitor[3].T + genericAHU.preheater.dynamicHX.heatCapacitor[4].T + genericAHU.preheater.dynamicHX.heatCapacitor[5].T + genericAHU.preheater.dynamicHX.vol1[1].dynBal.mC[1] + genericAHU.preheater.dynamicHX.vol1[1].dynBal.medium.Xi[1] + genericAHU.preheater.dynamicHX.vol1[1].dynBal.U + genericAHU.preheater.dynamicHX.vol1[2].dynBal.mC[1] + genericAHU.preheater.dynamicHX.vol1[2].dynBal.medium.Xi[1] + genericAHU.preheater.dynamicHX.vol1[2].dynBal.U + genericAHU.preheater.dynamicHX.vol1[3].dynBal.mC[1] + genericAHU.preheater.dynamicHX.vol1[3].dynBal.medium.Xi[1] + genericAHU.preheater.dynamicHX.vol1[3].dynBal.U + genericAHU.preheater.dynamicHX.vol1[4].dynBal.mC[1] + genericAHU.preheater.dynamicHX.vol1[4].dynBal.medium.Xi[1] + genericAHU.preheater.dynamicHX.vol1[4].dynBal.U + genericAHU.preheater.dynamicHX.vol1[5].dynBal.mC[1] + genericAHU.preheater.dynamicHX.vol1[5].dynBal.medium.Xi[1] + genericAHU.preheater.dynamicHX.vol1[5].dynBal.U + genericAHU.preheater.dynamicHX.vol2[1].dynBal.U + genericAHU.preheater.dynamicHX.vol2[2].dynBal.U + genericAHU.preheater.dynamicHX.vol2[3].dynBal.U + genericAHU.preheater.dynamicHX.vol2[4].dynBal.U + genericAHU.preheater.dynamicHX.vol2[5].dynBal.U + genericAHU.preheater.hydraulicModule.junc456.dynBal.U + genericAHU.preheater.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.del.x + genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.timDel.x + genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U + genericAHU.preheater.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U + genericAHU.preheater.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.del.x + genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.timDel.x + genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U + genericAHU.preheater.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U + genericAHU.preheater.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.del.x + genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.timDel.x + genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U + genericAHU.preheater.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U + genericAHU.preheater.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.del.x + genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.timDel.x + genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U + genericAHU.preheater.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U + genericAHU.preheater.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.del.x + genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.timDel.x + genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U + genericAHU.preheater.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U + genericAHU.preheater.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.del.x + genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.timDel.x + genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U + genericAHU.preheater.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U + genericAHU.preheater.hydraulicModule.PT1_a1.y + genericAHU.preheater.hydraulicModule.PT1_a2.y + genericAHU.preheater.hydraulicModule.PT1_b1.y + genericAHU.preheater.hydraulicModule.PT1_b2.y + genericAHU.preheater.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] + genericAHU.preheater.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] + genericAHU.preheater.hydraulicModule.senT_a1.T + genericAHU.preheater.hydraulicModule.senT_a2.T + genericAHU.preheater.hydraulicModule.senT_b1.T + genericAHU.preheater.hydraulicModule.senT_b2.T + genericAHU.preheater.hydraulicModule.valve.filter.s[1] + genericAHU.preheater.hydraulicModule.valve.vol.dynBal.U + genericAHU.preheater.PT1_airIn.y + genericAHU.preheater.PT1_airOut.y + genericAHU.preheater.senT_airIn.T + genericAHU.preheater.senT_airOut.T + genericAHU.PT1_airIn.y + genericAHU.PT1_airIn1.y + genericAHU.PT1_airIn2.y + genericAHU.PT1_airIn3.y + genericAHU.senRelHumSup.phi + genericAHU.senRelHumSup1.phi + genericAHU.senTExh.T + genericAHU.senTOda.T + genericAHU.senTRet.T + genericAHU.senTSup.T + thermalZone.ROM.extWallRC.thermCapExt[1].T + thermalZone.ROM.intWallRC.thermCapInt[1].T + thermalZone.ROM.volMoiAir.dynBal.m + thermalZone.ROM.volMoiAir.dynBal.mC[1] + thermalZone.ROM.volMoiAir.dynBal.medium.Xi[1] + thermalZone.ROM.volMoiAir.dynBal.U + thermalZone.ventCont.dEMA.ExpAVG.x[1] + thermalZone.ventCont.dEMA.ExpAVG1.x[1] + +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Examples.DemandControlledAHU.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Throttle"); +Check of AixLib.Systems.HydraulicModules.Example.Throttle: +The model has the same number of unknowns and equations: 962 +The model could not be deduced to be symbolically well-posed. +The model has + 944+Throttle.pipe1.simplePipe.vol[1].dynBal.nPorts+Throttle.pipe1.simplePipe.vol[2].dynBal.nPorts +Throttle.pipe1.simplePipe.vol[3].dynBal.nPorts+Throttle.pipe2.simplePipe.vol[1].dynBal.nPorts +Throttle.pipe2.simplePipe.vol[2].dynBal.nPorts+Throttle.pipe2.simplePipe.vol[3].dynBal.nPorts +Throttle.pipe3.simplePipe.vol[1].dynBal.nPorts+Throttle.pipe3.simplePipe.vol[2].dynBal.nPorts +Throttle.pipe3.simplePipe.vol[3].dynBal.nPorts +scalar unknowns and + 889+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Throttle.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not Throttle.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Throttle.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not Throttle.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not Throttle.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Throttle.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not Throttle.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not Throttle.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Throttle.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not Throttle.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not Throttle.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Throttle.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not Throttle.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Throttle.pipe3.simplePipe.vol[3].dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 962 +Check of AixLib.Systems.HydraulicModules.Example.Throttle successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Throttle.mos\",", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Throttle\",", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Throttle\\\");\",", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Throttle.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Throttle.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Throttle", tolerance=1e-6, stopTime=1000, resultFile="AixLib.Systems.HydraulicModules.Example.Throttle"); +Translation of AixLib.Systems.HydraulicModules.Example.Throttle: +The DAE has 962 scalar unknowns and 962 scalar equations. + +Statistics + +Original Model + Number of components: 204 + Variables: 2610 + Constants: 50 (50 scalars) + Parameters: 1264 (1222 scalars) + Unknowns: 1296 (996 scalars) + Differentiated variables: 39 scalars + Equations: 948 + Nontrivial: 749 +Translated Model + Constants: 917 scalars + Free parameters: 69 scalars + Parameter depending: 396 scalars + Outputs: 8 scalars + Continuous time states: 30 scalars + Time-varying variables: 210 scalars + Alias variables: 676 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {9} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {9, 1} + Sizes after manipulation of the nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + Throttle.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + Throttle.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Throttle.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Throttle.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Throttle.pipe1.simplePipe.vol[1].dynBal.U + Throttle.pipe1.simplePipe.vol[2].dynBal.U + Throttle.pipe1.simplePipe.vol[3].dynBal.U + Throttle.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + Throttle.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Throttle.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Throttle.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Throttle.pipe2.simplePipe.vol[1].dynBal.U + Throttle.pipe2.simplePipe.vol[2].dynBal.U + Throttle.pipe2.simplePipe.vol[3].dynBal.U + Throttle.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + Throttle.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Throttle.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Throttle.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Throttle.pipe3.simplePipe.vol[1].dynBal.U + Throttle.pipe3.simplePipe.vol[2].dynBal.U + Throttle.pipe3.simplePipe.vol[3].dynBal.U + Throttle.PT1_a1.y + Throttle.PT1_a2.y + Throttle.PT1_b1.y + Throttle.PT1_b2.y + Throttle.senT_a1.T + Throttle.senT_a2.T + Throttle.senT_b1.T + Throttle.senT_b2.T + Throttle.valve.filter.s[1] + +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Throttle.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Injection2WayValve"); +Check of AixLib.Systems.HydraulicModules.Example.Injection2WayValve: +The model has the same number of unknowns and equations: 2316 +The model could not be deduced to be symbolically well-posed. +The model has + 2266+Injection.PumpInterface.pump.vol.dynBal.nPorts+Injection.pipe1.simplePipe.vol[1].dynBal.nPorts +Injection.pipe1.simplePipe.vol[2].dynBal.nPorts+Injection.pipe1.simplePipe.vol[3].dynBal.nPorts +Injection.pipe2.simplePipe.vol[1].dynBal.nPorts+Injection.pipe2.simplePipe.vol[2].dynBal.nPorts +Injection.pipe2.simplePipe.vol[3].dynBal.nPorts+Injection.pipe3.simplePipe.vol[1].dynBal.nPorts +Injection.pipe3.simplePipe.vol[2].dynBal.nPorts+Injection.pipe3.simplePipe.vol[3].dynBal.nPorts +Injection.pipe4.simplePipe.vol[1].dynBal.nPorts+Injection.pipe4.simplePipe.vol[2].dynBal.nPorts +Injection.pipe4.simplePipe.vol[3].dynBal.nPorts+Injection.pipe5.simplePipe.vol[1].dynBal.nPorts +Injection.pipe5.simplePipe.vol[2].dynBal.nPorts+Injection.pipe5.simplePipe.vol[3].dynBal.nPorts +Injection.pipe6.simplePipe.vol[1].dynBal.nPorts+Injection.pipe6.simplePipe.vol[2].dynBal.nPorts +Injection.pipe6.simplePipe.vol[3].dynBal.nPorts+Injection.pipe7.simplePipe.vol[1].dynBal.nPorts +Injection.pipe7.simplePipe.vol[2].dynBal.nPorts+Injection.pipe7.simplePipe.vol[3].dynBal.nPorts +Injection.junc3v6.dynBal.nPorts+Injection.juncjp6.dynBal.nPorts +scalar unknowns and + 2132+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Injection.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3* Injection.PumpInterface.pump.vol.dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe3.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe4.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe4.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe4.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe5.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe5.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe5.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe6.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe6.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe6.simplePipe.vol[3].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe7.simplePipe.vol[1].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Injection.pipe7.simplePipe.vol[2].dynBal.nPorts+(if not Injection.pipe7.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Injection.pipe7.simplePipe.vol[3].dynBal.nPorts+(if not Injection.junc3v6.dynBal.use_mWat_flow then 1 else 0)+3*Injection.junc3v6.dynBal.nPorts +(if not Injection.juncjp6.dynBal.use_mWat_flow then 1 else 0)+3* Injection.juncjp6.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2316 +Check of AixLib.Systems.HydraulicModules.Example.Injection2WayValve successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Injection2WayValve.mos\",", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Injection2WayValve\",", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Injection2WayValve\\\");\",", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Injection2WayValve.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Injection2WayValve.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Injection2WayValve", tolerance=1e-6, stopTime=800, resultFile="AixLib.Systems.HydraulicModules.Example.Injection2WayValve"); +Translation of AixLib.Systems.HydraulicModules.Example.Injection2WayValve: +The DAE has 2316 scalar unknowns and 2316 scalar equations. + +Statistics + +Original Model + Number of components: 512 + Variables: 6229 + Constants: 121 (121 scalars) + Parameters: 3000 (3117 scalars) + Unknowns: 3108 (2406 scalars) + Differentiated variables: 87 scalars + Equations: 2272 + Nontrivial: 1746 +Translated Model + Constants: 2281 scalars + Free parameters: 149 scalars + Parameter depending: 1075 scalars + Outputs: 12 scalars + Continuous time states: 63 scalars + Time-varying variables: 515 scalars + Alias variables: 1624 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {21} + Sizes after manipulation of the nonlinear systems: {2} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {21, 1, 1} + Sizes after manipulation of the nonlinear systems: {3, 0, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + Injection.junc3v6.dynBal.U + Injection.juncjp6.dynBal.U + Injection.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe1.simplePipe.vol[1].dynBal.U + Injection.pipe1.simplePipe.vol[2].dynBal.U + Injection.pipe1.simplePipe.vol[3].dynBal.U + Injection.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe2.simplePipe.vol[1].dynBal.U + Injection.pipe2.simplePipe.vol[2].dynBal.U + Injection.pipe2.simplePipe.vol[3].dynBal.U + Injection.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe3.simplePipe.vol[1].dynBal.U + Injection.pipe3.simplePipe.vol[2].dynBal.U + Injection.pipe3.simplePipe.vol[3].dynBal.U + Injection.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe4.simplePipe.vol[1].dynBal.U + Injection.pipe4.simplePipe.vol[2].dynBal.U + Injection.pipe4.simplePipe.vol[3].dynBal.U + Injection.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe5.simplePipe.vol[1].dynBal.U + Injection.pipe5.simplePipe.vol[2].dynBal.U + Injection.pipe5.simplePipe.vol[3].dynBal.U + Injection.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe6.simplePipe.vol[1].dynBal.U + Injection.pipe6.simplePipe.vol[2].dynBal.U + Injection.pipe6.simplePipe.vol[3].dynBal.U + Injection.pipe7.Insulation.CylindricLoad1.heatCapacitor.T + Injection.pipe7.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Injection.pipe7.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Injection.pipe7.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Injection.pipe7.simplePipe.vol[1].dynBal.U + Injection.pipe7.simplePipe.vol[2].dynBal.U + Injection.pipe7.simplePipe.vol[3].dynBal.U + Injection.PT1_a1.y + Injection.PT1_a2.y + Injection.PT1_b1.y + Injection.PT1_b2.y + Injection.PumpInterface.pump.filter.s[1] + Injection.PumpInterface.pump.filter.s[2] + Injection.PumpInterface.pump.vol.dynBal.U + Injection.senT_a1.T + Injection.senT_a2.T + Injection.senT_b1.T + Injection.senT_b2.T + Injection.valve.filter.s[1] + +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Injection2WayValve.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Validation.AHU2_Heater"); +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Heater: +The model has the same number of unknowns and equations: 2418 +The model could not be deduced to be symbolically well-posed. +The model has + 2341+max([size(combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+ registerModule.hydraulicModule.valve.vol.dynBal.nPorts+registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.junc456.dynBal.nPorts+2*size(registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+2*registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+ registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+2* registerModule.dynamicHX.vol1[1].dynBal.nPorts+2*registerModule.dynamicHX.vol1[2].dynBal.nPorts +2*registerModule.dynamicHX.vol1[3].dynBal.nPorts+2*registerModule.dynamicHX.vol1[4].dynBal.nPorts +registerModule.dynamicHX.vol2[1].dynBal.nPorts+registerModule.dynamicHX.vol2[2].dynBal.nPorts +registerModule.dynamicHX.vol2[3].dynBal.nPorts+registerModule.dynamicHX.vol2[4].dynBal.nPorts +scalar unknowns and + 2193+(if boundaryWaterSource.use_Xi_in then 1 else (if boundaryWaterSource.use_X_in then 0 else 1))+(if not boundaryWaterSource.use_p_in then 1 else 0)+2* boundaryWaterSource.nPorts+(if not boundaryWaterSource.use_T_in then 1 else 0) +(if boundaryWaterSink.use_Xi_in then 1 else (if boundaryWaterSink.use_X_in then 0 else 1))+(if not boundaryWaterSink.use_p_in then 1 else 0)+2* boundaryWaterSink.nPorts+(if not boundaryWaterSink.use_T_in then 1 else 0)+( if boundaryAirSource.use_Xi_in then 2 else (if boundaryAirSource.use_X_in then 1 else 3))+3*boundaryAirSource.nPorts+(if not boundaryAirSource.use_m_flow_in then 1 else 0)+(if not boundaryAirSource.use_T_in then 1 else 0)+(if boundaryAirSink.use_Xi_in then 2 else (if boundaryAirSink.use_X_in then 1 else 3))+3*boundaryAirSink.nPorts+(if not boundaryAirSink.use_p_in then 1 else 0)+(if not boundaryAirSink.use_T_in then 1 else 0)+max([size( combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+2*size( registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.junc456.dynBal.nPorts+(if not registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +(if not registerModule.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +5*registerModule.dynamicHX.vol1[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+5* registerModule.dynamicHX.vol1[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[4].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[4].dynBal.nPorts+(if not registerModule.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3 *registerModule.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2418 +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Heater successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Heater.mos\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Validation.AHU2_Heater\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Validation.AHU2_Heater\\\");\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Validation.AHU2_Heater.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Heater.mos"); +simulateModel("AixLib.Systems.ModularAHU.Validation.AHU2_Heater", tolerance=1e-6, outputInterval=1, stopTime=4320, resultFile="AixLib.Systems.ModularAHU.Validation.AHU2_Heater"); +Translation of AixLib.Systems.ModularAHU.Validation.AHU2_Heater: +The DAE has 2418 scalar unknowns and 2418 scalar equations. + +Statistics + +Original Model + Number of components: 464 + Variables: 6155 + Constants: 125 (125 scalars) + Parameters: 2790 (12497 scalars) + Unknowns: 3240 (2521 scalars) + Differentiated variables: 86 scalars + Equations: 2514 + Nontrivial: 1950 +Translated Model + Constants: 2293 scalars + Free parameters: 5007 scalars + Parameter depending: 5640 scalars + Outputs: 17 scalars + Continuous time states: 62 scalars + Time-varying variables: 627 scalars + Alias variables: 1576 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {17, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {2, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {17, 1} + Sizes after manipulation of the nonlinear systems: {3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + registerModule.dynamicHX.heatCapacitor[1].T + registerModule.dynamicHX.heatCapacitor[2].T + registerModule.dynamicHX.heatCapacitor[3].T + registerModule.dynamicHX.heatCapacitor[4].T + registerModule.dynamicHX.vol1[1].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[1].dynBal.U + registerModule.dynamicHX.vol1[2].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[2].dynBal.U + registerModule.dynamicHX.vol1[3].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[3].dynBal.U + registerModule.dynamicHX.vol1[4].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[4].dynBal.U + registerModule.dynamicHX.vol2[1].dynBal.U + registerModule.dynamicHX.vol2[2].dynBal.U + registerModule.dynamicHX.vol2[3].dynBal.U + registerModule.dynamicHX.vol2[4].dynBal.U + registerModule.hydraulicModule.junc456.dynBal.U + registerModule.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe1.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe1.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe2.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe2.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe3.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe3.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe4.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe4.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe5.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe5.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe6.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe6.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.PT1_a1.y + registerModule.hydraulicModule.PT1_a2.y + registerModule.hydraulicModule.PT1_b1.y + registerModule.hydraulicModule.PT1_b2.y + registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] + registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] + registerModule.hydraulicModule.senT_a1.T + registerModule.hydraulicModule.senT_a2.T + registerModule.hydraulicModule.senT_b1.T + registerModule.hydraulicModule.senT_b2.T + registerModule.hydraulicModule.valve.vol.dynBal.U + registerModule.PT1_airIn.y + registerModule.PT1_airOut.y + registerModule.senT_airIn.T + registerModule.senT_airOut.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Validation.AHU2_Heater.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback"); +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback: +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.m_flow. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-2-6zo_7k0k/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.dp. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-2-6zo_7k0k/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +The model has the same number of unknowns and equations: 745 +The model could not be deduced to be symbolically well-posed. +The model has + 712+modularBoiler.boilerGeneric.vol.dynBal.nPorts+2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1 +2*modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3+2* modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.offDesignOperation.boilerEffciency.nin +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n1+2* modularBoiler.boilerGeneric.designOperation.multiplex4.n2+2*modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +2*modularBoiler.boilerGeneric.designOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.boilerEffciency.nin +modularBoiler.pump.vol.dynBal.nPorts+modularBoiler.val.vol.dynBal.nPorts+ vol.dynBal.nPorts +scalar unknowns and + 693+2*(modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n1+ modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n2+modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n3 +modularBoiler.boilerGeneric.offDesignOperation.multiplex4.n4+modularBoiler.boilerGeneric.designOperation.multiplex4.n1 +modularBoiler.boilerGeneric.designOperation.multiplex4.n2+modularBoiler.boilerGeneric.designOperation.multiplex4.n3 +modularBoiler.boilerGeneric.designOperation.multiplex4.n4)+(if bou.use_Xi_in then 1 else (if bou.use_X_in then 0 else 1))+(if not bou.use_p_in then 1 else 0)+2*bou.nPorts+(if not bou.use_T_in then 1 else 0)+(if not modularBoiler.boilerGeneric.vol.dynBal.use_mWat_flow then 1 else 0)+3* modularBoiler.boilerGeneric.vol.dynBal.nPorts+(if not modularBoiler.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3*modularBoiler.pump.vol.dynBal.nPorts+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts+(if not modularBoiler.val.vol.dynBal.use_mWat_flow then 1 else 0)+3*modularBoiler.val.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 745 +Check of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback successful. +Warning: WARNINGS have been issued. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerFeedback.mos\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback\\\");\",", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerFeedback.mos"); +simulateModel("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback", tolerance=1e-06, stopTime=20000, method="dassl", resultFile="AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback"); +Translation of AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback: +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.m_flow. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-2-6zo_7k0k/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +Warning: Non-literal value. +In nominal attribute for modularBoiler.boilerGeneric.preDro.dp. +Ignoring nominal attribute. +In class Modelica.Units.SI. + Near file: /opt/dymola-2022-x86_64/Modelica/Library/Modelica 4.0.0/Units.mo, line 237 +Used in base-class modularBoiler.boilerGeneric.preDro.PartialTwoPortInterface. + Near file: /tmp/tmp-AixLib-2-6zo_7k0k/AixLib/Fluid/BaseClasses/PartialResistance.mo, line 3 +The DAE has 745 scalar unknowns and 745 scalar equations. +Warning: The initial conditions are not fully specified. +Dymola has selected default initial conditions. +Warning: Assuming fixed start value for the continuous states: + vol.dynBal.U(start = 4165531.824*(vol.dynBal.fluidVolume*(vol.dynBal.T_start -273.15))) + + +Statistics + +Original Model + Number of components: 192 + Variables: 1742 + Constants: 29 (29 scalars) + Parameters: 856 (976 scalars) + Unknowns: 857 (771 scalars) + Differentiated variables: 18 scalars + Equations: 759 + Nontrivial: 630 +Translated Model + Constants: 559 scalars + Free parameters: 172 scalars + Parameter depending: 359 scalars + Outputs: 11 scalars + Continuous time states: 13 scalars + Time-varying variables: 195 scalars + Alias variables: 491 scalars + Assumed default initial conditions: 1 + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {4} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {8} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + modularBoiler.boilerControl.feedbackControl.PIValve.I.y + modularBoiler.boilerControl.internalFirRatControl.PID.I.y + modularBoiler.boilerGeneric.senTRet.T + modularBoiler.boilerGeneric.senTSup.T + modularBoiler.boilerGeneric.vol.dynBal.U + modularBoiler.pump.filter.s[1] + modularBoiler.pump.filter.s[2] + modularBoiler.pump.vol.dynBal.U + modularBoiler.senTRet.T + modularBoiler.senTSup.T + modularBoiler.val.vol.dynBal.U + senTRet.T + vol.dynBal.U + +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularEnergySystems.ModularBoiler.Examples.ModularBoilerFeedback.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Examples.GenericAHU"); +Check of AixLib.Systems.ModularAHU.Examples.GenericAHU: +The model has the same number of unknowns and equations: 9000 +The model could not be deduced to be symbolically well-posed. +The model has + 8800+genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+2*genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts +genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts+genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts+2*genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts +genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts +genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts+2*genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts +genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts +2*genericAHU.dynamicHX.vol1[1].dynBal.nPorts+2*genericAHU.dynamicHX.vol1[2].dynBal.nPorts +2*genericAHU.dynamicHX.vol2[1].dynBal.nPorts+2*genericAHU.dynamicHX.vol2[2].dynBal.nPorts +2*genericAHU.fanSup.vol.dynBal.nPorts+2*genericAHU.fanRet.vol.dynBal.nPorts+2 *genericAHU.humidifier.vol.dynBal.nPorts+2*genericAHU.humidifierRet.vol.dynBal.nPorts +scalar unknowns and + 8285+(if not genericAHU.humidifier.steamHumidifier then 1 else 0)+(if boundaryOutsideAir.use_Xi_in then 2 else (if boundaryOutsideAir.use_X_in then 1 else 3))+boundaryOutsideAir.nPorts+(if not boundaryOutsideAir.use_p_in then 1 else 0)+boundaryOutsideAir.nPorts+(if not boundaryOutsideAir.use_T_in then 1 else 0)+boundaryOutsideAir.nPorts+(if boundarySupplyAir.use_Xi_in then 2 else (if boundarySupplyAir.use_X_in then 1 else 3))+boundarySupplyAir.nPorts+ (if not boundarySupplyAir.use_p_in then 1 else 0)+boundarySupplyAir.nPorts+( if not boundarySupplyAir.use_T_in then 1 else 0)+boundarySupplyAir.nPorts+( if boundaryExhaustAir.use_Xi_in then 2 else (if boundaryExhaustAir.use_X_in then 1 else 3))+boundaryExhaustAir.nPorts+(if not boundaryExhaustAir.use_p_in then 1 else 0)+boundaryExhaustAir.nPorts+(if not boundaryExhaustAir.use_T_in then 1 else 0)+boundaryExhaustAir.nPorts+(if boundaryReturnAir.use_Xi_in then 2 else (if boundaryReturnAir.use_X_in then 1 else 3))+boundaryReturnAir.nPorts +(if not boundaryReturnAir.use_p_in then 1 else 0)+boundaryReturnAir.nPorts+( if not boundaryReturnAir.use_T_in then 1 else 0)+boundaryReturnAir.nPorts+( if SourcePreheater.use_Xi_in then 1 else (if SourcePreheater.use_X_in then 0 else 1))+(if not SourcePreheater.use_p_in then 1 else 0)+SourcePreheater.nPorts +(if not SourcePreheater.use_T_in then 1 else 0)+SourcePreheater.nPorts+(if SinkPreheater.use_Xi_in then 1 else (if SinkPreheater.use_X_in then 0 else 1)) +(if not SinkPreheater.use_p_in then 1 else 0)+SinkPreheater.nPorts+(if not SinkPreheater.use_T_in then 1 else 0)+SinkPreheater.nPorts+(if SourceCooler.use_Xi_in then 1 else (if SourceCooler.use_X_in then 0 else 1))+( if not SourceCooler.use_p_in then 1 else 0)+SourceCooler.nPorts+(if not SourceCooler.use_T_in then 1 else 0)+SourceCooler.nPorts+(if SinkCooler.use_Xi_in then 1 else (if SinkCooler.use_X_in then 0 else 1))+(if not SinkCooler.use_p_in then 1 else 0)+SinkCooler.nPorts+(if not SinkCooler.use_T_in then 1 else 0)+ SinkCooler.nPorts+(if SourceHeater.use_Xi_in then 1 else (if SourceHeater.use_X_in then 0 else 1))+(if not SourceHeater.use_p_in then 1 else 0)+ SourceHeater.nPorts+(if not SourceHeater.use_T_in then 1 else 0)+ SourceHeater.nPorts+(if SinkHeater.use_Xi_in then 1 else (if SinkHeater.use_X_in then 0 else 1))+(if not SinkHeater.use_p_in then 1 else 0)+SinkHeater.nPorts +(if not SinkHeater.use_T_in then 1 else 0)+SinkHeater.nPorts+(if not genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+ (if not genericAHU.preheater.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.preheater.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts+( if not genericAHU.preheater.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+3* genericAHU.preheater.dynamicHX.vol1[1].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts+3* genericAHU.preheater.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.preheater.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.preheater.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.cooler.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.cooler.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+2 *genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.cooler.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.cooler.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts+3* genericAHU.cooler.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.cooler.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.cooler.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts +2*genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.nPorts+( if not genericAHU.heater.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+2* genericAHU.heater.hydraulicModule.junc456.dynBal.nPorts+(if not genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts +2*genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+2 *genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts+3*genericAHU.heater.dynamicHX.vol1[1].dynBal.nPorts +(if not genericAHU.heater.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts+3* genericAHU.heater.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.heater.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts+2* genericAHU.heater.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.dynamicHX.vol1[1].dynBal.nPorts+3* genericAHU.dynamicHX.vol1[1].dynBal.nPorts+(if not genericAHU.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.dynamicHX.vol1[2].dynBal.nPorts+3* genericAHU.dynamicHX.vol1[2].dynBal.nPorts+(if not genericAHU.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.dynamicHX.vol2[1].dynBal.nPorts+3* genericAHU.dynamicHX.vol2[1].dynBal.nPorts+(if not genericAHU.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.dynamicHX.vol2[2].dynBal.nPorts+3* genericAHU.dynamicHX.vol2[2].dynBal.nPorts+(if not genericAHU.fanSup.vol.dynBal.use_mWat_flow then 1 else 0)+2*genericAHU.fanSup.vol.dynBal.nPorts+3*genericAHU.fanSup.vol.dynBal.nPorts +(if not genericAHU.fanRet.vol.dynBal.use_mWat_flow then 1 else 0)+2* genericAHU.fanRet.vol.dynBal.nPorts+3*genericAHU.fanRet.vol.dynBal.nPorts+2* genericAHU.humidifier.vol.dynBal.nPorts+3*genericAHU.humidifier.vol.dynBal.nPorts +2*genericAHU.humidifierRet.vol.dynBal.nPorts+3*genericAHU.humidifierRet.vol.dynBal.nPorts +(if not genericAHU.preheater.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+2 *genericAHU.preheater.hydraulicModule.valve.vol.dynBal.nPorts+(if not genericAHU.cooler.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0) +genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts+2*genericAHU.cooler.hydraulicModule.valve.vol.dynBal.nPorts +(if not genericAHU.heater.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts+2* genericAHU.heater.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 9000 +Check of AixLib.Systems.ModularAHU.Examples.GenericAHU successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/GenericAHU.mos\",", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Examples.GenericAHU\",", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Examples.GenericAHU\\\");\",", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Examples.GenericAHU.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Examples/GenericAHU.mos"); +simulateModel("AixLib.Systems.ModularAHU.Examples.GenericAHU", stopTime=7200, method="dassl", tolerance=1e-6, resultFile="AixLib.Systems.ModularAHU.Examples.GenericAHU"); +Translation of AixLib.Systems.ModularAHU.Examples.GenericAHU: +The DAE has 9000 scalar unknowns and 9000 scalar equations. +Redundant consistent initial conditions. +Removed the following equations which are redundant and consistent: + genericAHU.preheater.dynamicHX.vol1[2].p_start = genericAHU.preheater.dynamicHX.p1_start; + genericAHU.cooler.dynamicHX.vol1[1].p_start = genericAHU.cooler.dynamicHX.p1_start; + genericAHU.heater.dynamicHX.vol1[2].p_start = genericAHU.heater.dynamicHX.p1_start; + genericAHU.dynamicHX.vol1[1].p_start = genericAHU.dynamicHX.p1_start; + genericAHU.dynamicHX.vol2[1].p_start = genericAHU.dynamicHX.p2_start; + genericAHU.fanSup.vol.p_start = genericAHU.fanSup.p_start; + genericAHU.humidifier.vol.p_start = genericAHU.humidifier.p_start; + if (genericAHU.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. FixedInitial) then + if (genericAHU.dynamicHX.vol1[2].dynBal.initialize_p) then + genericAHU.dynamicHX.vol1[2].dynBal.medium.p = genericAHU.dynamicHX.vol1[2].dynBal.p_start; + end if; + else + if (genericAHU.dynamicHX.vol1[2].dynBal.massDynamics == Modelica.Fluid.Types.Dynamics. SteadyStateInitial) then + if (genericAHU.dynamicHX.vol1[2].dynBal.initialize_p) then + der(genericAHU.dynamicHX.vol1[2].dynBal.medium.p) = 0; + end if; + end if; + end if; + +This required evaluation of +the interactive parameters + boundaryExhaustAir.p(start = 101325) + boundarySupplyAir.p(start = 101325) + genericAHU.dynamicHX.p1_start(start = 101325) + genericAHU.fanSup.dp_start(start = 0) + genericAHU.fanSup.p_start(start = 101325) + genericAHU.humidifier.p_start(start = 101325) + +The redundancies involve +initial equations: + genericAHU.fanSup.filter.y = genericAHU.fanSup.filter.y_start; + genericAHU.dampHX.port_a.p = genericAHU.preheater.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.dampHX.port_a.p = genericAHU.preheater.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.cooler.port_b1.p = genericAHU.cooler.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.cooler.port_b1.p = genericAHU.cooler.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.heater.port_b1.p = genericAHU.heater.dynamicHX.vol1[1].dynBal.p_start; + genericAHU.heater.port_b1.p = genericAHU.heater.dynamicHX.vol1[2].dynBal.p_start; + boundaryExhaustAir.p = genericAHU.dynamicHX.vol1[1].dynBal.p_start; + boundaryExhaustAir.p = genericAHU.dynamicHX.vol1[2].dynBal.p_start; + genericAHU.cooler.port_a1.p = genericAHU.dynamicHX.vol2[1].dynBal.p_start; + genericAHU.cooler.port_a1.p = genericAHU.dynamicHX.vol2[2].dynBal.p_start; + genericAHU.fanSup.port_a.p = genericAHU.fanSup.vol.dynBal.p_start; + genericAHU.fanSup.port_a.p = genericAHU.humidifier.vol.dynBal.p_start; + +Sparse solver handling possible: false. +Due to flag Advanced.SparseActivate=false. +Model sparse and large enough: true. +Sparse solvers are available for dassl, lsodar, cvode, radau, esdirk*, sdirk* (using OpenMP, set number of cores with Advanced.NumberOfCores). + +Statistics + +Original Model + Number of components: 1899 + Variables: 23029 + Constants: 457 (457 scalars) + Parameters: 10980 (11860 scalars) + Unknowns: 11592 (9419 scalars) + Differentiated variables: 337 scalars + Equations: 8571 + Nontrivial: 6714 +Translated Model + Constants: 8236 scalars + Free parameters: 846 scalars + Parameter depending: 4221 scalars + Continuous time states: 260 scalars + Time-varying variables: 2222 scalars + Alias variables: 6211 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {3, 3, 3, 3, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {1, 1, 1, 3, 1, 4, 1, 1, 1, 18, 18, 18} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 1, 0, 1, 0, 0, 0, 2, 2, 2} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {1, 1, 1, 3, 1, 4, 1, 1, 18, 1, 18, 1, 18, 1} + Sizes after manipulation of the nonlinear systems: {0, 0, 0, 1, 0, 1, 0, 0, 3, 0, 3, 0, 3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + ctrAHUBasic.ctrCo.PID.D.x + ctrAHUBasic.ctrCo.PID.I.y + ctrAHUBasic.ctrPh.PID.D.x + ctrAHUBasic.ctrPh.PID.I.y + ctrAHUBasic.ctrRh.PID.D.x + ctrAHUBasic.ctrRh.PID.I.y + ctrAHUBasic.PID_VflowRet.D.x + ctrAHUBasic.PID_VflowRet.I.y + ctrAHUBasic.PID_VflowSup.D.x + ctrAHUBasic.PID_VflowSup.I.y + genericAHU.cooler.dynamicHX.heatCapacitor[1].T + genericAHU.cooler.dynamicHX.heatCapacitor[2].T + genericAHU.cooler.dynamicHX.vol1[1].dynBal.medium.Xi[1] + genericAHU.cooler.dynamicHX.vol1[1].dynBal.U + genericAHU.cooler.dynamicHX.vol1[2].dynBal.medium.Xi[1] + genericAHU.cooler.dynamicHX.vol1[2].dynBal.U + genericAHU.cooler.dynamicHX.vol2[1].dynBal.U + genericAHU.cooler.dynamicHX.vol2[2].dynBal.U + genericAHU.cooler.hydraulicModule.junc456.dynBal.U + genericAHU.cooler.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.U + genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.U + genericAHU.cooler.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.U + genericAHU.cooler.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.U + genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.U + genericAHU.cooler.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.U + genericAHU.cooler.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.U + genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.U + genericAHU.cooler.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.U + genericAHU.cooler.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.U + genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.U + genericAHU.cooler.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.U + genericAHU.cooler.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.U + genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.U + genericAHU.cooler.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.U + genericAHU.cooler.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.U + genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.U + genericAHU.cooler.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.U + genericAHU.cooler.hydraulicModule.PT1_a1.y + genericAHU.cooler.hydraulicModule.PT1_a2.y + genericAHU.cooler.hydraulicModule.PT1_b1.y + genericAHU.cooler.hydraulicModule.PT1_b2.y + genericAHU.cooler.hydraulicModule.PumpInterface.pump.filter.s[1] + genericAHU.cooler.hydraulicModule.PumpInterface.pump.filter.s[2] + genericAHU.cooler.hydraulicModule.PumpInterface.pump.vol.dynBal.U + genericAHU.cooler.hydraulicModule.senT_a1.T + genericAHU.cooler.hydraulicModule.senT_a2.T + genericAHU.cooler.hydraulicModule.senT_b1.T + genericAHU.cooler.hydraulicModule.senT_b2.T + genericAHU.cooler.hydraulicModule.valve.filter.s[1] + genericAHU.cooler.hydraulicModule.valve.vol.dynBal.U + genericAHU.cooler.port_a1.p + genericAHU.cooler.port_b1.p + genericAHU.cooler.PT1_airIn.y + genericAHU.cooler.PT1_airOut.y + genericAHU.cooler.senT_airIn.T + genericAHU.cooler.senT_airOut.T + genericAHU.dampBypass.filter.s[1] + genericAHU.dampBypass.filter.s[2] + genericAHU.dampHX.filter.s[1] + genericAHU.dampHX.filter.s[2] + genericAHU.dampHX.port_a.p + genericAHU.dynamicHX.heatCapacitor[1].T + genericAHU.dynamicHX.heatCapacitor[2].T + genericAHU.dynamicHX.vol1[1].dynBal.medium.Xi[1] + genericAHU.dynamicHX.vol1[1].dynBal.U + genericAHU.dynamicHX.vol1[2].dynBal.medium.Xi[1] + genericAHU.dynamicHX.vol1[2].dynBal.U + genericAHU.dynamicHX.vol2[1].dynBal.medium.Xi[1] + genericAHU.dynamicHX.vol2[1].dynBal.U + genericAHU.dynamicHX.vol2[2].dynBal.medium.Xi[1] + genericAHU.dynamicHX.vol2[2].dynBal.U + genericAHU.fanRet.filter.s[1] + genericAHU.fanRet.filter.s[2] + genericAHU.fanRet.vol.dynBal.m + genericAHU.fanRet.vol.dynBal.medium.Xi[1] + genericAHU.fanRet.vol.dynBal.U + genericAHU.fanSup.filter.s[1] + genericAHU.fanSup.filter.s[2] + genericAHU.fanSup.vol.dynBal.medium.Xi[1] + genericAHU.fanSup.vol.dynBal.U + genericAHU.flapRet.filter.s[1] + genericAHU.flapRet.filter.s[2] + genericAHU.flapSup.filter.s[1] + genericAHU.flapSup.filter.s[2] + genericAHU.heater.dynamicHX.heatCapacitor[1].T + genericAHU.heater.dynamicHX.heatCapacitor[2].T + genericAHU.heater.dynamicHX.vol1[1].dynBal.medium.Xi[1] + genericAHU.heater.dynamicHX.vol1[1].dynBal.U + genericAHU.heater.dynamicHX.vol1[2].dynBal.medium.Xi[1] + genericAHU.heater.dynamicHX.vol1[2].dynBal.U + genericAHU.heater.dynamicHX.vol2[1].dynBal.U + genericAHU.heater.dynamicHX.vol2[2].dynBal.U + genericAHU.heater.hydraulicModule.junc456.dynBal.U + genericAHU.heater.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.U + genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.U + genericAHU.heater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.U + genericAHU.heater.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.U + genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.U + genericAHU.heater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.U + genericAHU.heater.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.U + genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.U + genericAHU.heater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.U + genericAHU.heater.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.U + genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.U + genericAHU.heater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.U + genericAHU.heater.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.U + genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.U + genericAHU.heater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.U + genericAHU.heater.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.U + genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.U + genericAHU.heater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.U + genericAHU.heater.hydraulicModule.PT1_a1.y + genericAHU.heater.hydraulicModule.PT1_a2.y + genericAHU.heater.hydraulicModule.PT1_b1.y + genericAHU.heater.hydraulicModule.PT1_b2.y + genericAHU.heater.hydraulicModule.PumpInterface.pump.filter.s[1] + genericAHU.heater.hydraulicModule.PumpInterface.pump.filter.s[2] + genericAHU.heater.hydraulicModule.PumpInterface.pump.vol.dynBal.U + genericAHU.heater.hydraulicModule.senT_a1.T + genericAHU.heater.hydraulicModule.senT_a2.T + genericAHU.heater.hydraulicModule.senT_b1.T + genericAHU.heater.hydraulicModule.senT_b2.T + genericAHU.heater.hydraulicModule.valve.filter.s[1] + genericAHU.heater.hydraulicModule.valve.vol.dynBal.U + genericAHU.heater.port_b1.p + genericAHU.heater.PT1_airIn.y + genericAHU.heater.PT1_airOut.y + genericAHU.heater.senT_airIn.T + genericAHU.heater.senT_airOut.T + genericAHU.humidifier.vol.dynBal.medium.Xi[1] + genericAHU.humidifier.vol.dynBal.U + genericAHU.humidifierRet.vol.dynBal.m + genericAHU.humidifierRet.vol.dynBal.medium.Xi[1] + genericAHU.humidifierRet.vol.dynBal.U + genericAHU.preheater.dynamicHX.heatCapacitor[1].T + genericAHU.preheater.dynamicHX.heatCapacitor[2].T + genericAHU.preheater.dynamicHX.vol1[1].dynBal.medium.Xi[1] + genericAHU.preheater.dynamicHX.vol1[1].dynBal.U + genericAHU.preheater.dynamicHX.vol1[2].dynBal.medium.Xi[1] + genericAHU.preheater.dynamicHX.vol1[2].dynBal.U + genericAHU.preheater.dynamicHX.vol2[1].dynBal.U + genericAHU.preheater.dynamicHX.vol2[2].dynBal.U + genericAHU.preheater.hydraulicModule.junc456.dynBal.U + genericAHU.preheater.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[1].dynBal.U + genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[2].dynBal.U + genericAHU.preheater.hydraulicModule.pipe1.simplePipe.vol[3].dynBal.U + genericAHU.preheater.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[1].dynBal.U + genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[2].dynBal.U + genericAHU.preheater.hydraulicModule.pipe2.simplePipe.vol[3].dynBal.U + genericAHU.preheater.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[1].dynBal.U + genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[2].dynBal.U + genericAHU.preheater.hydraulicModule.pipe3.simplePipe.vol[3].dynBal.U + genericAHU.preheater.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[1].dynBal.U + genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[2].dynBal.U + genericAHU.preheater.hydraulicModule.pipe4.simplePipe.vol[3].dynBal.U + genericAHU.preheater.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[1].dynBal.U + genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[2].dynBal.U + genericAHU.preheater.hydraulicModule.pipe5.simplePipe.vol[3].dynBal.U + genericAHU.preheater.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[1].dynBal.U + genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[2].dynBal.U + genericAHU.preheater.hydraulicModule.pipe6.simplePipe.vol[3].dynBal.U + genericAHU.preheater.hydraulicModule.PT1_a1.y + genericAHU.preheater.hydraulicModule.PT1_a2.y + genericAHU.preheater.hydraulicModule.PT1_b1.y + genericAHU.preheater.hydraulicModule.PT1_b2.y + genericAHU.preheater.hydraulicModule.PumpInterface.pump.filter.s[1] + genericAHU.preheater.hydraulicModule.PumpInterface.pump.filter.s[2] + genericAHU.preheater.hydraulicModule.PumpInterface.pump.vol.dynBal.U + genericAHU.preheater.hydraulicModule.senT_a1.T + genericAHU.preheater.hydraulicModule.senT_a2.T + genericAHU.preheater.hydraulicModule.senT_b1.T + genericAHU.preheater.hydraulicModule.senT_b2.T + genericAHU.preheater.hydraulicModule.valve.filter.s[1] + genericAHU.preheater.hydraulicModule.valve.vol.dynBal.U + genericAHU.preheater.PT1_airIn.y + genericAHU.preheater.PT1_airOut.y + genericAHU.preheater.senT_airIn.T + genericAHU.preheater.senT_airOut.T + genericAHU.PT1_airIn.y + genericAHU.PT1_airIn1.y + genericAHU.PT1_airIn2.y + genericAHU.PT1_airIn3.y + genericAHU.senRelHumSup.phi + genericAHU.senRelHumSup1.phi + genericAHU.senTExh.T + genericAHU.senTOda.T + genericAHU.senTRet.T + genericAHU.senTSup.T + +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Examples.GenericAHU.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.Admix"); +Check of AixLib.Systems.HydraulicModules.Example.Admix: +The model has the same number of unknowns and equations: 2088 +The model could not be deduced to be symbolically well-posed. +The model has + 2044+Admix.valve.vol.dynBal.nPorts+Admix.pipe1.simplePipe.vol[1].dynBal.nPorts+ Admix.pipe1.simplePipe.vol[2].dynBal.nPorts+Admix.pipe1.simplePipe.vol[3].dynBal.nPorts +Admix.pipe2.simplePipe.vol[1].dynBal.nPorts+Admix.pipe2.simplePipe.vol[2].dynBal.nPorts +Admix.pipe2.simplePipe.vol[3].dynBal.nPorts+Admix.pipe3.simplePipe.vol[1].dynBal.nPorts +Admix.pipe3.simplePipe.vol[2].dynBal.nPorts+Admix.pipe3.simplePipe.vol[3].dynBal.nPorts +Admix.pipe4.simplePipe.vol[1].dynBal.nPorts+Admix.pipe4.simplePipe.vol[2].dynBal.nPorts +Admix.pipe4.simplePipe.vol[3].dynBal.nPorts+Admix.pipe5.simplePipe.vol[1].dynBal.nPorts +Admix.pipe5.simplePipe.vol[2].dynBal.nPorts+Admix.pipe5.simplePipe.vol[3].dynBal.nPorts +Admix.pipe6.simplePipe.vol[1].dynBal.nPorts+Admix.pipe6.simplePipe.vol[2].dynBal.nPorts +Admix.pipe6.simplePipe.vol[3].dynBal.nPorts+Admix.junc456.dynBal.nPorts+ Admix.PumpInterface.pump.vol.dynBal.nPorts +scalar unknowns and + 1925+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not Admix.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe3.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe4.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe4.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe4.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe5.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe5.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe5.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe5.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe5.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe5.simplePipe.vol[3].dynBal.nPorts+(if not Admix.pipe6.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe6.simplePipe.vol[1].dynBal.nPorts+(if not Admix.pipe6.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* Admix.pipe6.simplePipe.vol[2].dynBal.nPorts+(if not Admix.pipe6.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*Admix.pipe6.simplePipe.vol[3].dynBal.nPorts+(if not Admix.junc456.dynBal.use_mWat_flow then 1 else 0)+3*Admix.junc456.dynBal.nPorts +(if not Admix.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3* Admix.PumpInterface.pump.vol.dynBal.nPorts+(if not Admix.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3*Admix.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2088 +Check of AixLib.Systems.HydraulicModules.Example.Admix successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Admix.mos\",", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.Admix\",", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.Admix\\\");\",", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.Admix.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/Admix.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.Admix", tolerance=1e-6, stopTime=800, resultFile="AixLib.Systems.HydraulicModules.Example.Admix"); +Translation of AixLib.Systems.HydraulicModules.Example.Admix: +The DAE has 2088 scalar unknowns and 2088 scalar equations. + +Statistics + +Original Model + Number of components: 467 + Variables: 5670 + Constants: 111 (111 scalars) + Parameters: 2755 (2949 scalars) + Unknowns: 2804 (2171 scalars) + Differentiated variables: 77 scalars + Equations: 2056 + Nontrivial: 1589 +Translated Model + Constants: 2081 scalars + Free parameters: 168 scalars + Parameter depending: 1054 scalars + Outputs: 12 scalars + Continuous time states: 56 scalars + Time-varying variables: 471 scalars + Alias variables: 1457 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {19} + Sizes after manipulation of the nonlinear systems: {2} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {19, 1} + Sizes after manipulation of the nonlinear systems: {3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + Admix.junc456.dynBal.U + Admix.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + Admix.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Admix.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Admix.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Admix.pipe1.simplePipe.vol[1].dynBal.U + Admix.pipe1.simplePipe.vol[2].dynBal.U + Admix.pipe1.simplePipe.vol[3].dynBal.U + Admix.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + Admix.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Admix.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Admix.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Admix.pipe2.simplePipe.vol[1].dynBal.U + Admix.pipe2.simplePipe.vol[2].dynBal.U + Admix.pipe2.simplePipe.vol[3].dynBal.U + Admix.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + Admix.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Admix.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Admix.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Admix.pipe3.simplePipe.vol[1].dynBal.U + Admix.pipe3.simplePipe.vol[2].dynBal.U + Admix.pipe3.simplePipe.vol[3].dynBal.U + Admix.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + Admix.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Admix.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Admix.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Admix.pipe4.simplePipe.vol[1].dynBal.U + Admix.pipe4.simplePipe.vol[2].dynBal.U + Admix.pipe4.simplePipe.vol[3].dynBal.U + Admix.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + Admix.pipe5.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Admix.pipe5.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Admix.pipe5.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Admix.pipe5.simplePipe.vol[1].dynBal.U + Admix.pipe5.simplePipe.vol[2].dynBal.U + Admix.pipe5.simplePipe.vol[3].dynBal.U + Admix.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + Admix.pipe6.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + Admix.pipe6.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + Admix.pipe6.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + Admix.pipe6.simplePipe.vol[1].dynBal.U + Admix.pipe6.simplePipe.vol[2].dynBal.U + Admix.pipe6.simplePipe.vol[3].dynBal.U + Admix.PT1_a1.y + Admix.PT1_a2.y + Admix.PT1_b1.y + Admix.PT1_b2.y + Admix.PumpInterface.pump.filter.s[1] + Admix.PumpInterface.pump.filter.s[2] + Admix.PumpInterface.pump.vol.dynBal.U + Admix.senT_a1.T + Admix.senT_a2.T + Admix.senT_b1.T + Admix.senT_b2.T + Admix.valve.filter.s[1] + Admix.valve.vol.dynBal.U + +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.Admix.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.ModularAHU.Validation.AHU2_Preheater"); +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Preheater: +The model has the same number of unknowns and equations: 2556 +The model could not be deduced to be symbolically well-posed. +The model has + 2471+max([size(combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+ registerModule.hydraulicModule.valve.vol.dynBal.nPorts+registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts+ registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts+ registerModule.hydraulicModule.junc456.dynBal.nPorts+2*size(registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+2*registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+2* registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+ registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts+2* registerModule.dynamicHX.vol1[1].dynBal.nPorts+2*registerModule.dynamicHX.vol1[2].dynBal.nPorts +2*registerModule.dynamicHX.vol1[3].dynBal.nPorts+2*registerModule.dynamicHX.vol1[4].dynBal.nPorts +2*registerModule.dynamicHX.vol1[5].dynBal.nPorts+registerModule.dynamicHX.vol2[1].dynBal.nPorts +registerModule.dynamicHX.vol2[2].dynBal.nPorts+registerModule.dynamicHX.vol2[3].dynBal.nPorts +registerModule.dynamicHX.vol2[4].dynBal.nPorts+registerModule.dynamicHX.vol2[5].dynBal.nPorts +scalar unknowns and + 2311+(if boundaryWaterSource.use_Xi_in then 1 else (if boundaryWaterSource.use_X_in then 0 else 1))+(if not boundaryWaterSource.use_p_in then 1 else 0)+2* boundaryWaterSource.nPorts+(if not boundaryWaterSource.use_T_in then 1 else 0) +(if boundaryWaterSink.use_Xi_in then 1 else (if boundaryWaterSink.use_X_in then 0 else 1))+(if not boundaryWaterSink.use_p_in then 1 else 0)+2* boundaryWaterSink.nPorts+(if not boundaryWaterSink.use_T_in then 1 else 0)+( if boundaryAirSource.use_Xi_in then 2 else (if boundaryAirSource.use_X_in then 1 else 3))+3*boundaryAirSource.nPorts+(if not boundaryAirSource.use_m_flow_in then 1 else 0)+(if not boundaryAirSource.use_T_in then 1 else 0)+(if boundaryAirSink.use_Xi_in then 2 else (if boundaryAirSink.use_X_in then 1 else 3))+3*boundaryAirSink.nPorts+(if not boundaryAirSink.use_p_in then 1 else 0)+(if not boundaryAirSink.use_T_in then 1 else 0)+max([size( combiTimeTable.columns, 1); size(combiTimeTable.offset, 1)])+2*size( registerModule.hydraulicModule.PumpInterface.physics.maxMinTable.columns, 1)+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n1+ registerModule.hydraulicModule.PumpInterface.physics.deMultiplex2.n2+ registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.n+(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.nPorts +(if not registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.nPorts +(if not registerModule.hydraulicModule.junc456.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.junc456.dynBal.nPorts+(if not registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.use_mWat_flow then 1 else 0)+3*registerModule.hydraulicModule.PumpInterface.physics.vol.dynBal.nPorts +(if not registerModule.dynamicHX.vol1[1].dynBal.use_mWat_flow then 1 else 0) +5*registerModule.dynamicHX.vol1[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[2].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[3].dynBal.use_mWat_flow then 1 else 0)+5* registerModule.dynamicHX.vol1[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[4].dynBal.use_mWat_flow then 1 else 0)+5*registerModule.dynamicHX.vol1[4].dynBal.nPorts+(if not registerModule.dynamicHX.vol1[5].dynBal.use_mWat_flow then 1 else 0)+5* registerModule.dynamicHX.vol1[5].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[1].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[1].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[2].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[2].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[3].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[3].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[4].dynBal.use_mWat_flow then 1 else 0)+3* registerModule.dynamicHX.vol2[4].dynBal.nPorts+(if not registerModule.dynamicHX.vol2[5].dynBal.use_mWat_flow then 1 else 0)+3*registerModule.dynamicHX.vol2[5].dynBal.nPorts+(if not registerModule.hydraulicModule.valve.vol.dynBal.use_mWat_flow then 1 else 0)+3 *registerModule.hydraulicModule.valve.vol.dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 2556 +Check of AixLib.Systems.ModularAHU.Validation.AHU2_Preheater successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Preheater.mos\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.ModularAHU.Validation.AHU2_Preheater\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.ModularAHU.Validation.AHU2_Preheater\\\");\",", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularAHU/Validation/AHU2_Preheater.mos"); +simulateModel("AixLib.Systems.ModularAHU.Validation.AHU2_Preheater", tolerance=1e-6, outputInterval=1, stopTime=7200, resultFile="AixLib.Systems.ModularAHU.Validation.AHU2_Preheater"); +Translation of AixLib.Systems.ModularAHU.Validation.AHU2_Preheater: +The DAE has 2556 scalar unknowns and 2556 scalar equations. + +Statistics + +Original Model + Number of components: 487 + Variables: 6441 + Constants: 133 (133 scalars) + Parameters: 2896 (27364 scalars) + Unknowns: 3412 (2665 scalars) + Differentiated variables: 92 scalars + Equations: 2638 + Nontrivial: 2035 +Translated Model + Constants: 2471 scalars + Free parameters: 17889 scalars + Parameter depending: 7469 scalars + Outputs: 17 scalars + Continuous time states: 66 scalars + Time-varying variables: 665 scalars + Alias variables: 1668 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {17, 6, 6, 6, 6, 6, 6} + Sizes after manipulation of the nonlinear systems: {2, 1, 1, 1, 1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {17, 1} + Sizes after manipulation of the nonlinear systems: {3, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + registerModule.dynamicHX.heatCapacitor[1].T + registerModule.dynamicHX.heatCapacitor[2].T + registerModule.dynamicHX.heatCapacitor[3].T + registerModule.dynamicHX.heatCapacitor[4].T + registerModule.dynamicHX.heatCapacitor[5].T + registerModule.dynamicHX.vol1[1].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[1].dynBal.U + registerModule.dynamicHX.vol1[2].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[2].dynBal.U + registerModule.dynamicHX.vol1[3].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[3].dynBal.U + registerModule.dynamicHX.vol1[4].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[4].dynBal.U + registerModule.dynamicHX.vol1[5].dynBal.medium.Xi[1] + registerModule.dynamicHX.vol1[5].dynBal.U + registerModule.dynamicHX.vol2[1].dynBal.U + registerModule.dynamicHX.vol2[2].dynBal.U + registerModule.dynamicHX.vol2[3].dynBal.U + registerModule.dynamicHX.vol2[4].dynBal.U + registerModule.dynamicHX.vol2[5].dynBal.U + registerModule.hydraulicModule.junc456.dynBal.U + registerModule.hydraulicModule.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe1.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe1.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe1.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe2.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe2.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe2.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe3.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe3.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe3.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe4.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe4.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe4.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe5.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe5.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe5.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe5.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.pipe6.Insulation.CylindricLoad1.heatCapacitor.T + registerModule.hydraulicModule.pipe6.plugFlowPipe.del.x + registerModule.hydraulicModule.pipe6.plugFlowPipe.timDel.x + registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_a.dynBal.U + registerModule.hydraulicModule.pipe6.plugFlowPipe.vol_b.dynBal.U + registerModule.hydraulicModule.PT1_a1.y + registerModule.hydraulicModule.PT1_a2.y + registerModule.hydraulicModule.PT1_b1.y + registerModule.hydraulicModule.PT1_b2.y + registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[1] + registerModule.hydraulicModule.PumpInterface.physics.criticalDamping.x[2] + registerModule.hydraulicModule.senT_a1.T + registerModule.hydraulicModule.senT_a2.T + registerModule.hydraulicModule.senT_b1.T + registerModule.hydraulicModule.senT_b2.T + registerModule.hydraulicModule.valve.vol.dynBal.U + registerModule.PT1_airIn.y + registerModule.PT1_airOut.y + registerModule.senT_airIn.T + registerModule.senT_airOut.T + +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.ModularAHU.Validation.AHU2_Preheater.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HydraulicModules.Example.ThrottlePump"); +Check of AixLib.Systems.HydraulicModules.Example.ThrottlePump: +The model has the same number of unknowns and equations: 1396 +The model could not be deduced to be symbolically well-posed. +The model has + 1370+ThrottlePump.PumpInterface.pump.vol.dynBal.nPorts+ThrottlePump.pipe1.simplePipe.vol[1].dynBal.nPorts +ThrottlePump.pipe1.simplePipe.vol[2].dynBal.nPorts+ThrottlePump.pipe1.simplePipe.vol[3].dynBal.nPorts +ThrottlePump.pipe2.simplePipe.vol[1].dynBal.nPorts+ThrottlePump.pipe2.simplePipe.vol[2].dynBal.nPorts +ThrottlePump.pipe2.simplePipe.vol[3].dynBal.nPorts+ThrottlePump.pipe3.simplePipe.vol[1].dynBal.nPorts +ThrottlePump.pipe3.simplePipe.vol[2].dynBal.nPorts+ThrottlePump.pipe3.simplePipe.vol[3].dynBal.nPorts +ThrottlePump.pipe4.simplePipe.vol[1].dynBal.nPorts+ThrottlePump.pipe4.simplePipe.vol[2].dynBal.nPorts +ThrottlePump.pipe4.simplePipe.vol[3].dynBal.nPorts +scalar unknowns and + 1295+(if boundary.use_Xi_in then 1 else (if boundary.use_X_in then 0 else 1))+( if not boundary.use_p_in then 1 else 0)+2*boundary.nPorts+(if not boundary.use_T_in then 1 else 0)+(if boundary1.use_Xi_in then 1 else (if boundary1.use_X_in then 0 else 1))+(if not boundary1.use_p_in then 1 else 0)+2 *boundary1.nPorts+(if not boundary1.use_T_in then 1 else 0)+(if not ThrottlePump.PumpInterface.pump.vol.dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.PumpInterface.pump.vol.dynBal.nPorts+(if not ThrottlePump.pipe1.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe1.simplePipe.vol[1].dynBal.nPorts+(if not ThrottlePump.pipe1.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe1.simplePipe.vol[2].dynBal.nPorts+(if not ThrottlePump.pipe1.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe1.simplePipe.vol[3].dynBal.nPorts+(if not ThrottlePump.pipe2.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe2.simplePipe.vol[1].dynBal.nPorts+(if not ThrottlePump.pipe2.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe2.simplePipe.vol[2].dynBal.nPorts+(if not ThrottlePump.pipe2.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe2.simplePipe.vol[3].dynBal.nPorts+(if not ThrottlePump.pipe3.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe3.simplePipe.vol[1].dynBal.nPorts+(if not ThrottlePump.pipe3.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe3.simplePipe.vol[2].dynBal.nPorts+(if not ThrottlePump.pipe3.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe3.simplePipe.vol[3].dynBal.nPorts+(if not ThrottlePump.pipe4.simplePipe.vol[1].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe4.simplePipe.vol[1].dynBal.nPorts+(if not ThrottlePump.pipe4.simplePipe.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*ThrottlePump.pipe4.simplePipe.vol[2].dynBal.nPorts+(if not ThrottlePump.pipe4.simplePipe.vol[3].dynBal.use_mWat_flow then 1 else 0)+3* ThrottlePump.pipe4.simplePipe.vol[3].dynBal.nPorts +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 1396 +Check of AixLib.Systems.HydraulicModules.Example.ThrottlePump successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/ThrottlePump.mos\",", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HydraulicModules.Example.ThrottlePump\",", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HydraulicModules.Example.ThrottlePump\\\");\",", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HydraulicModules.Example.ThrottlePump.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HydraulicModules/Examples/ThrottlePump.mos"); +simulateModel("AixLib.Systems.HydraulicModules.Example.ThrottlePump", tolerance=1e-6, stopTime=600, resultFile="AixLib.Systems.HydraulicModules.Example.ThrottlePump"); +Translation of AixLib.Systems.HydraulicModules.Example.ThrottlePump: +The DAE has 1396 scalar unknowns and 1396 scalar equations. + +Statistics + +Original Model + Number of components: 315 + Variables: 3779 + Constants: 71 (71 scalars) + Parameters: 1848 (2020 scalars) + Unknowns: 1860 (1450 scalars) + Differentiated variables: 53 scalars + Equations: 1378 + Nontrivial: 1079 +Translated Model + Constants: 1400 scalars + Free parameters: 120 scalars + Parameter depending: 731 scalars + Outputs: 12 scalars + Continuous time states: 40 scalars + Time-varying variables: 312 scalars + Alias variables: 978 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {5, 2, 5, 2, 5, 2, 5, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {14} + Sizes after manipulation of the nonlinear systems: {1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of nonlinear systems of equations: {14, 1} + Sizes after manipulation of the nonlinear systems: {1, 0} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + ThrottlePump.pipe1.Insulation.CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe1.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe1.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe1.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe1.simplePipe.vol[1].dynBal.U + ThrottlePump.pipe1.simplePipe.vol[2].dynBal.U + ThrottlePump.pipe1.simplePipe.vol[3].dynBal.U + ThrottlePump.pipe2.Insulation.CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe2.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe2.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe2.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe2.simplePipe.vol[1].dynBal.U + ThrottlePump.pipe2.simplePipe.vol[2].dynBal.U + ThrottlePump.pipe2.simplePipe.vol[3].dynBal.U + ThrottlePump.pipe3.Insulation.CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe3.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe3.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe3.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe3.simplePipe.vol[1].dynBal.U + ThrottlePump.pipe3.simplePipe.vol[2].dynBal.U + ThrottlePump.pipe3.simplePipe.vol[3].dynBal.U + ThrottlePump.pipe4.Insulation.CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe4.simplePipe.PipeWall[1].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe4.simplePipe.PipeWall[2].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe4.simplePipe.PipeWall[3].CylindricLoad1.heatCapacitor.T + ThrottlePump.pipe4.simplePipe.vol[1].dynBal.U + ThrottlePump.pipe4.simplePipe.vol[2].dynBal.U + ThrottlePump.pipe4.simplePipe.vol[3].dynBal.U + ThrottlePump.PT1_a1.y + ThrottlePump.PT1_a2.y + ThrottlePump.PT1_b1.y + ThrottlePump.PT1_b2.y + ThrottlePump.PumpInterface.pump.filter.s[1] + ThrottlePump.PumpInterface.pump.filter.s[2] + ThrottlePump.PumpInterface.pump.vol.dynBal.U + ThrottlePump.senT_a1.T + ThrottlePump.senT_a2.T + ThrottlePump.senT_b1.T + ThrottlePump.senT_b2.T + ThrottlePump.valve.filter.s[1] + +Finished + = true + + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HydraulicModules.Example.ThrottlePump.translation.log"); = true + + +rCheck = checkModel("AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem"); +Check of AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem: +The model has the same number of unknowns and equations: 1727 +The model could not be deduced to be symbolically well-posed. +The model has + 1641+2*rad.nEle+6*size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.tableMerge, 1)+2*(if heatPumpSystem.use_opeEnvFroRec then size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.dataTable.tableUppBou, 1) else size(heatPumpSystem.tableUpp, 1))+6*size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.boundaryMap.tableMerge, 1)+2*(if heatPumpSystem.use_opeEnvFroRec then size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.boundaryMap.dataTable.tableUppBou, 1) else size(heatPumpSystem.tableUpp, 1))+vol.dynBal.nPorts+max([size( timTab.columns, 1); size(timTab.offset, 1)])+rad.vol[1].dynBal.nPorts+ rad.vol[2].dynBal.nPorts+rad.vol[3].dynBal.nPorts+rad.vol[4].dynBal.nPorts+ rad.vol[5].dynBal.nPorts+rad.sumCon.nin+rad.sumRad.nin+heatPumpSystem.heatPump.con.vol.dynBal.nPorts +heatPumpSystem.heatPump.eva.vol.dynBal.nPorts+2*heatPumpSystem.nthOrder+ heatPumpSystem.pumSin.vol.dynBal.nPorts+heatPumpSystem.pumSou.vol.dynBal.nPorts +size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.boundaryMap.uppCombiTable1Ds.columns, 1)+heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.boundaryMap.nor1.nu +heatPumpSystem.hPSystemController.safetyControl.onOffController.orSetN.nu+ heatPumpSystem.hPSystemController.multiSum.nu +scalar unknowns and + 1594+max([size(timTab.columns, 1); size(timTab.offset, 1)])+(if preSou.use_Xi_in then 1 else (if preSou.use_X_in then 0 else 1))+(if not preSou.use_p_in then 1 else 0)+2*preSou.nPorts+(if not preSou.use_T_in then 1 else 0)+(if weaDat.pAtmSou == AixLib.BoundaryConditions.Types.DataSource.Parameter then 1 else 0)+(if weaDat.TDewPoiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TDryBulSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.TBlaSkySou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.relHumSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.opaSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.ceiHeiSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.totSkyCovSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winSpeSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.winDirSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HInfHorSou == AixLib.BoundaryConditions.Types.DataSource. Parameter then 1 else 0)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HDifHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HDirNor_HGloHor then 2 else 1)+(if weaDat.HSou == AixLib.BoundaryConditions.Types.RadiationDataSource. Input_HGloHor_HDifHor then 2 else 1)+(if sou.use_Xi_in then 1 else (if sou.use_X_in then 0 else 1))+(if not sou.use_p_in then 1 else 0)+2*sou.nPorts +(if not sou.use_T_in then 1 else 0)+(if sin.use_Xi_in then 1 else (if sin.use_X_in then 0 else 1))+(if not sin.use_p_in then 1 else 0)+2*sin.nPorts +(if not sin.use_T_in then 1 else 0)+size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.boundaryMap.uppCombiTable1Ds.columns, 1)+(if not vol.dynBal.use_mWat_flow then 1 else 0)+3*vol.dynBal.nPorts+(if not rad.vol[1].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[1].dynBal.nPorts +(if not rad.vol[2].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[2].dynBal.nPorts +(if not rad.vol[3].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[3].dynBal.nPorts +(if not rad.vol[4].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[4].dynBal.nPorts +(if not rad.vol[5].dynBal.use_mWat_flow then 1 else 0)+3*rad.vol[5].dynBal.nPorts +(if not heatPumpSystem.heatPump.con.vol.dynBal.use_mWat_flow then 1 else 0)+3 *heatPumpSystem.heatPump.con.vol.dynBal.nPorts+(if not heatPumpSystem.heatPump.eva.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatPumpSystem.heatPump.eva.vol.dynBal.nPorts+2* heatPumpSystem.nthOrder+(if not heatPumpSystem.pumSin.vol.dynBal.use_mWat_flow then 1 else 0)+3*heatPumpSystem.pumSin.vol.dynBal.nPorts+(if not heatPumpSystem.pumSou.vol.dynBal.use_mWat_flow then 1 else 0)+3* heatPumpSystem.pumSou.vol.dynBal.nPorts+2*rad.nEle+6*size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.tableMerge, 1)+2*(if heatPumpSystem.use_opeEnvFroRec then size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.dataTable.tableUppBou, 1) else size(heatPumpSystem.tableUpp, 1))+6*size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.boundaryMap.tableMerge, 1)+2*(if heatPumpSystem.use_opeEnvFroRec then size(heatPumpSystem.hPSystemController.safetyControl.operationalEnvelope.boundaryMap.dataTable.tableUppBou, 1) else size(heatPumpSystem.tableUpp, 1)) +scalar equations. +However, exploiting the given numerical settings of parameters gives the same number of unknowns and equations: + 1727 +Check of AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem successful. +Declaring variable: Boolean rCheck ; + +Modelica.Utilities.Streams.print(" { \"file\" : \"AixLib/Resources/Scripts/Dymola/Systems/HeatPumpSystems/Examples/HeatPumpSystem.mos\",", "AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"model\" : \"AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem\",", "AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"check\" : {", "AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"command\" : \"checkModel(\\\"AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem\\\");\",", "AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log"); +Modelica.Utilities.Streams.print(" \"result\" : " + String(rCheck), "AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log"); +Modelica.Utilities.Streams.print(" },", "AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem.statistics.log"); + + +rScript=RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/HeatPumpSystems/Examples/HeatPumpSystem.mos"); +simulateModel("AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem", stopTime=86400, method="dassl", tolerance=1e-06, resultFile="AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem"); +Translation of AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem: +The DAE has 1727 scalar unknowns and 1727 scalar equations. +Warning: The conditions of the following assert statements are always false: +Warning: assert(heatPumpSystem.heatPump.con.preDro.homotopyInitialization, "In HeatPumpSystem.heatPumpSystem.heatPump.con.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning); + The variable heatPumpSystem.heatPump.con.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-3-wgcn1fjk/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component heatPumpSystem.heatPump.con.preDro.PartialResistance. +Warning: assert(heatPumpSystem.heatPump.eva.preDro.homotopyInitialization, "In HeatPumpSystem.heatPumpSystem.heatPump.eva.preDro: The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.", AssertionLevel.warning); + The variable heatPumpSystem.heatPump.eva.preDro.homotopyInitialization = false, was declared in class AixLib.Fluid.BaseClasses.PartialResistance, /tmp/tmp-AixLib-3-wgcn1fjk/AixLib/Fluid/BaseClasses/PartialResistance.mo at line 12, and used in component heatPumpSystem.heatPump.eva.preDro.PartialResistance. + +Statistics + +Original Model + Number of components: 450 + Variables: 3942 + Constants: 85 (177 scalars) + Parameters: 1836 (3744 scalars) + Unknowns: 2021 (1774 scalars) + Differentiated variables: 40 scalars + Equations: 1713 + Nontrivial: 1417 +Translated Model + Constants: 1888 scalars + Free parameters: 555 scalars + Parameter depending: 1815 scalars + Outputs: 24 scalars + Continuous time states: 30 scalars + Time-varying variables: 381 scalars + Alias variables: 1056 scalars + Number of mixed real/discrete systems of equations: 0 + Sizes of linear systems of equations: {2, 2, 2, 2, 2, 6, 2} + Sizes after manipulation of the linear systems: {0, 0, 0, 0, 0, 0, 0} + Sizes of nonlinear systems of equations: {3, 1, 1} + Sizes after manipulation of the nonlinear systems: {1, 1, 1} + Number of numerical Jacobians: 0 + Initialization problem + Sizes of linear systems of equations: {2} + Sizes after manipulation of the linear systems: {0} + Sizes of nonlinear systems of equations: {11, 1, 1} + Sizes after manipulation of the nonlinear systems: {5, 1, 1} + Number of numerical Jacobians: 0 + +Selected continuous time states +Statically selected continuous time states + heaCap.T + heatPumpSystem.heatPump.con.heatCap.T + heatPumpSystem.heatPump.con.vol.dynBal.U + heatPumpSystem.heatPump.eva.heatCap.T + heatPumpSystem.heatPump.eva.vol.dynBal.U + heatPumpSystem.heatPump.heatFlowIneCon.x[1] + heatPumpSystem.heatPump.heatFlowIneCon.x[2] + heatPumpSystem.heatPump.heatFlowIneCon.x[3] + heatPumpSystem.heatPump.heatFlowIneEva.x[1] + heatPumpSystem.heatPump.heatFlowIneEva.x[2] + heatPumpSystem.heatPump.heatFlowIneEva.x[3] + heatPumpSystem.heatPump.senT_a1.T + heatPumpSystem.heatPump.senT_a2.T + heatPumpSystem.heatPump.senT_b1.T + heatPumpSystem.heatPump.senT_b2.T + heatPumpSystem.hPSystemController.calcCOP.movAve.uInt.y + heatPumpSystem.hPSystemController.hPControls.ConvTSetToNSet.movAve.uInt.y + heatPumpSystem.pumSin.filter.s[1] + heatPumpSystem.pumSin.filter.s[2] + heatPumpSystem.pumSin.vol.dynBal.U + heatPumpSystem.pumSou.filter.s[1] + heatPumpSystem.pumSou.filter.s[2] + heatPumpSystem.pumSou.vol.dynBal.U + rad.vol[1].dynBal.U + rad.vol[2].dynBal.U + rad.vol[3].dynBal.U + rad.vol[4].dynBal.U + rad.vol[5].dynBal.U + senT_a1.T + vol.dynBal.m + +Warning: WARNINGS have been issued. +Finished + = true + +Declaring variable: Boolean rScript ; + +savelog("AixLib.Systems.HeatPumpSystems.Examples.HeatPumpSystem.translation.log"); \ No newline at end of file diff --git a/docs/issue1147_GenericBoiler/regression/Systems/unitTests-dymola.log b/docs/issue1147_GenericBoiler/regression/Systems/unitTests-dymola.log new file mode 100644 index 0000000000..e11f5674b6 --- /dev/null +++ b/docs/issue1147_GenericBoiler/regression/Systems/unitTests-dymola.log @@ -0,0 +1,14 @@ +Regression tests are only run for the following package: + AixLib.Systems +*** Warning: Unspecified initial conditions in 'RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerSimple.mos");'. + +*** Warning: Unspecified initial conditions in 'RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerHeatingCurve.mos");'. + +*** Warning: Unspecified initial conditions in 'RunScript("modelica://AixLib/Resources/Scripts/Dymola/Systems/ModularEnergySystems/Examples/ModularBoilerFeedback.mos");'. + +Comparison files output by funnel are stored in the directory 'funnel_comp' of size 1.1 MB. +Run 'python -c "import buildingspy.development.regressiontest as t; t.Tester(tool=\"dymola\").report()"' +to access a summary of the comparison results. + +Script that runs unit tests had 3 warnings and 0 errors. +