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Application of the VdW-711 equation of state to polar mixtures: correlation of binary and prediction of multicomponent vapour-liquid equilibria

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dc.contributor.author Kalospiros, NS en
dc.contributor.author Misseyannis, GM en
dc.contributor.author Androulakis, IP en
dc.contributor.author Tassios, DP en
dc.date.accessioned 2014-03-01T01:08:15Z
dc.date.available 2014-03-01T01:08:15Z
dc.date.issued 1991 en
dc.identifier.issn 0378-3812 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/10374
dc.relation.uri http://www.scopus.com/inward/record.url?eid=2-s2.0-0026174272&partnerID=40&md5=1e73f19c9a387fe0031b1d7eb6e61572 en
dc.subject.classification Thermodynamics en
dc.subject.classification Chemistry, Physical en
dc.subject.classification Engineering, Chemical en
dc.subject.other Mixtures en
dc.subject.other VLE Properties en
dc.subject.other Equations Of State en
dc.subject.other Thermodynamics en
dc.subject.other Gamma-Phi Approach en
dc.subject.other Gibbs Free Energy en
dc.subject.other UNIQUAC Model en
dc.subject.other VdW-711 Equation Of State en
dc.subject.other Mixtures en
dc.title Application of the VdW-711 equation of state to polar mixtures: correlation of binary and prediction of multicomponent vapour-liquid equilibria en
heal.type journalArticle en
heal.language English en
heal.publicationDate 1991 en
heal.abstract The VdW-711 equation of state for polar compounds of Androulakis et al. (1989) is combined with the UNIQUAC model for the excess Gibbs free energy to establish the mixing rule in the attractive term of the equation of state. The obtained model, applicable thus to both vapour and liquid phases, eliminates the uncertainty in estimating the vapour phase non-ideality, a serious problem in using the gamma-phi approach, especially at higher pressures. Application of the model: (i) the correlation of binary vapour-liquid equilibria (VLE) data of polar systems and (ii) the prediction of multicomponent VLE behaviour from binary data, gives very good results, comparable to those with the gamma-phi approach, in both cases. In addition, successful prediction of saturated liquid volumes is obtained. Prediction of liquid volumes of mixing is also discussed. © 1991. en
heal.publisher ELSEVIER SCIENCE BV en
heal.journalName Fluid Phase Equilibria en
dc.identifier.isi ISI:A1991FV99700011 en
dc.identifier.volume 64 en
dc.identifier.issue C en
dc.identifier.spage 173 en
dc.identifier.epage 184 en


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