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Application of the LCVM model to systems containing organic compounds and supercritical carbon dioxide

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dc.contributor.author Yakoumis, IV en
dc.contributor.author Vlachos, K en
dc.contributor.author Kontogeorgis, GM en
dc.contributor.author Coutsikos, P en
dc.contributor.author Kalospiros, NS en
dc.contributor.author Tassios, D en
dc.contributor.author Kolisis, FN en
dc.date.accessioned 2014-03-01T01:44:39Z
dc.date.available 2014-03-01T01:44:39Z
dc.date.issued 1996 en
dc.identifier.issn 08968446 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/24441
dc.relation.uri http://www.scopus.com/inward/record.url?eid=2-s2.0-0002326887&partnerID=40&md5=31a5c135a6120b1b61890a60c4266858 en
dc.subject Biotechnology en
dc.subject Carbon dioxide en
dc.subject EOS/GE model en
dc.subject Equation of state en
dc.subject Solubility en
dc.subject Vapor-liquid equilibria en
dc.title Application of the LCVM model to systems containing organic compounds and supercritical carbon dioxide en
heal.type journalArticle en
heal.publicationDate 1996 en
heal.abstract A recently developed equation of state-excess Gibbs free energy (EOS/GE) model with the LCVM (linear combination of Vidai and Michelsen) mixing rule, capable of successful VLE prediction in asymmetric systems is applied to the prediction of solubilities of alkenes, ethers, acids, alcohols, and esters in supercritical carbon dioxide. Considering the experimental uncertainties, excellent correlation of binary data and satisfactory prediction of ternary and multicomponent equilibria are obtained in most cases over a wide range of temperature, pressure, and system asymmetry. These promising results render the LCVM model a useful tool for the preliminary design of processes involving mixtures with organic compounds and supercritical carbon dioxide. en
heal.journalName Journal of Supercritical Fluids en
dc.identifier.volume 9 en
dc.identifier.issue 2 en
dc.identifier.spage 88 en
dc.identifier.epage 98 en


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