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Modeling phase equilibria for acid gas mixtures using the CPA equation of state. I. Mixtures with H<sub>2</sub>S
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References
2010
Year
EngineeringChemical CompositionPhase EquilibriaMethanolS MixturesAcid Gas MixturesChemistryBinary H 2Solution (Chemistry)Thermodynamic ModellingChemical EngineeringMolecular ThermodynamicsThermodynamicsPhase SeparationEquilibrium Thermodynamic PropertyH 2Chemical ThermodynamicsPhysical ChemistryCpa EquationHydrogenEnergyPhase EquilibriumEquilibrium ThermodynamicsInterfacial PhenomenaChemical KineticsI. Mixtures
Abstract The Cubic‐Plus‐Association (CPA) equation of state is applied to a large variety of mixtures containing H 2 S, which are of interest in the oil and gas industry. Binary H 2 S mixtures with alkanes, CO 2 , water, methanol, and glycols are first considered. The interactions of H 2 S with polar compounds (water, methanol, and glycols) are modeled assuming presence or not of cross‐association interactions. Such interactions are accounted for using either a combining rule or a cross‐solvation energy obtained from spectroscopic data. Using the parameters obtained from the binary systems, one ternary and three quaternary mixtures are considered. It is shown that overall excellent correlation for binary mixtures and satisfactory prediction results for multicomponent systems are obtained. There are significant differences between the various modeling approaches and the best results are obtained when cross association is explicitly accounted for, especially using the cross‐association energy from independent experimental studies rather than from combining rules. © 2010 American Institute of Chemical Engineers AIChE J, 2010
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