The Performance of EoS/G E Models in the Prediction of Vapor-Liquid Equilibria in Asymmetric Systems

By Voutsas E.C.   Boukouvalas C.J.   Kalospiros N.S.   Tassios D.P.  

Fluid Phase Equilibria, Vol. 116, Iss. 1, 1996-03 ,pp. : 480-487

Elsevier

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An implicit type EOS-G E(VP) model employing vapor pressure standard state I. Prediction of high-pressure vapor-liquid equilibria based on low temperature data

By Kurihara K.   Kojima K.  

Fluid Phase Equilibria, Vol. 113, Iss. 1, 1995-12 ,pp. : 27-43

Elsevier

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Calculation of vapor-liquid equilibria for a 10-component system: comparison of EOS, EOS-G E and G E -Henry's law models

By Patel N.C.   Abovsky V.   Watanasiri S.  

Fluid Phase Equilibria, Vol. 185, Iss. 1, 2001-07 ,pp. : 397-405

Elsevier

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Modelling of high-pressure phase equilibria using the Sako-Wu-Prausnitz equation of state II. Vapour-liquid equilibria and liquid-liquid equilibria in polyolefin systems

By Tork T.   Sadowski G.   Arlt W.   de Haan A.   Krooshof G.  

Fluid Phase Equilibria, Vol. 163, Iss. 1, 1999-09 ,pp. : 79-98

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Prediction of supercritical fluid-liquid equilibria for carbon dioxide and fish oil related compounds through the equation of state - excess function (EOS-g E ) approach

By Coniglio L.   Knudsen K.   Gani R.  

Fluid Phase Equilibria, Vol. 116, Iss. 1, 1996-03 ,pp. : 510-517

Elsevier

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