The code provides a combination of the bubble-point algorithm and Newton-Raphson algorithm following the Naphtali & Sandholm approach to simulate ideal hydrocarbon mixtures. The thermodynamic equilibrium and vapor and liquid enthalpies are calculated using the DIPPR equation set.
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This repository provides a combination of the bubble-point algorithm and Naphtali-Sandholm algorithm to steadily compute distillation separations with partial condensers
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