Prediction of liquid-liquid equilibria at high pressure for binary systems using EOS-G E models: methanol+hydrocarbon systems

By Matsuda H.   Kurihara K.   Ochi K.   Kojima K.  

Fluid Phase Equilibria, Vol. 203, Iss. 1, 2002-12 ,pp. : 269-284

Elsevier

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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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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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Vapor-liquid equilibrium predictions of refrigerant mixtures from a cubic equation of state with a G E -EoS mixing rule

By Ioannidis S.   Knox D.E.  

Fluid Phase Equilibria, Vol. 140, Iss. 1, 1997-12 ,pp. : 17-35

Elsevier

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