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 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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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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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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An EOS/G E type mixing rule for perturbed hard-sphere equation of state and its application to the calculation of solid solubility in supercritical carbon dioxide

By Chongli Z.   Masuoka H.  

Fluid Phase Equilibria, Vol. 141, Iss. 1, 1997-12 ,pp. : 13-23

Elsevier

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