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Vapor-liquid equilibria for alcohol/hydrocarbon systems using the CPA Equation of State

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dc.contributor.author Yakoumis, IV en
dc.contributor.author Kontogeorgis, GM en
dc.contributor.author Voutsas, EC en
dc.contributor.author Tassios, DP en
dc.date.accessioned 2014-03-01T01:13:29Z
dc.date.available 2014-03-01T01:13:29Z
dc.date.issued 1997 en
dc.identifier.issn 0378-3812 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/12510
dc.subject Alcohols en
dc.subject Application en
dc.subject Association en
dc.subject Hydrocarbons en
dc.subject Vapor-liquid equilibria en
dc.subject.classification Thermodynamics en
dc.subject.classification Chemistry, Physical en
dc.subject.classification Engineering, Chemical en
dc.subject.other Alcohols en
dc.subject.other Binary mixtures en
dc.subject.other Equations of state en
dc.subject.other Hydrocarbons en
dc.subject.other Perturbation techniques en
dc.subject.other Thermal effects en
dc.subject.other Cubic plus association equation of state (CPA EoS) en
dc.subject.other Soave Redlich Kwong (SRK) equation of state en
dc.subject.other Phase equilibria en
dc.title Vapor-liquid equilibria for alcohol/hydrocarbon systems using the CPA Equation of State en
heal.type journalArticle en
heal.identifier.primary 10.1016/S0378-3812(96)03200-1 en
heal.identifier.secondary http://dx.doi.org/10.1016/S0378-3812(96)03200-1 en
heal.language English en
heal.publicationDate 1997 en
heal.abstract The recently developed Cubic-Plus-Association Equation of State (CPA EoS) is extended in this study to binary systems containing one associating compound (alcohol) and an inert one (hydrocarbon). CPA combines the Soave-Redlich-Kwong (SRK) equation of state for the physical part with an association term based on perturbation theory. The classical van der Waals one-fluid mixing rules are used for the attractive and co-volume parameters, alpha and b, while the extension of the association term to mixtures is rigorous and does not require any mixing rules. Excellent correlation of Vapor-Liquid Equilibria (VLE) is obtained using a small value for the interaction parameter (k(ij)) in the attractive term of the physical part of the equation of state even when it is temperature-independent. CPA yields much better results than SRK and its performance is similar to that of other association models, like the Anderko EoS, and the more complex SAFT and Simplified SAFT EoS. (C) 1997 Elsevier Science B.V. en
heal.publisher ELSEVIER SCIENCE BV en
heal.journalName Fluid Phase Equilibria en
dc.identifier.doi 10.1016/S0378-3812(96)03200-1 en
dc.identifier.isi ISI:A1997XB29200003 en
dc.identifier.volume 130 en
dc.identifier.issue 1-2 en
dc.identifier.spage 31 en
dc.identifier.epage 47 en


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