Matching equation of state mixing rules to activity coefficient model expressions

Fluid Phase Equilibria

Volumn 121, Issue 1-2, 1996, Pages 15-26

  Michelsen, Michael L ^a  

^a TECHNICAL UNIVERSITY OF DENMARK   (Denmark)

Author keywords

[No Author keywords available]

Indexed keywords

EQUATIONS OF STATE; ERRORS; GIBBS FREE ENERGY; MATHEMATICAL MODELS; MIXTURES;

MIXING RULES; VOLATILITY; ZERO PRESSURE;

MIXING;

MIXING; THERMODYNAMICS;

EID: 0030184098     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/0378-3812(96)03020-8     Document Type: Article

References (13)

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2. Dahl, S. and Michelsen, M.L., 1990. High-pressure vapor-liquid equilibrium with a UNIFAC-based equation of state. AIChE. J., 36: 1829.
3. Dahl, S., Fredenslund, Aa, Rasmussen, P., 1991. The MHV-2 model: a UNIFAC-based equation of state model for prediction of gas solubility and vapor-liquid equilibrium at low and high pressures, Ind. Eng. Chem. Res., 30: 1936.
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9. Michelsen, M.L., 1990a. A method for incorporating excess Gibbs energy models in equations of state, Fluid Phase Equilibria, 60: 47.
10. Michelsen, M.L., 1990b. A modified Huron-Vidal mixing rule for cubic equations of state, Fluid Phase Equilibria, 60: 213.
11. Soave, G., 1972. Equilibrium constants from a modified Redlich-Kwong equation of state. Chem. Eng. Sci., 27: 1197.
12. Soave, G., 1992. A new expression of q(α) for the modified Huron-Vidal methods. Fluid Phase Equilibria, 72: 325.
13. Wong, D.S.H. and Sandler, S.I., 1992. A theoretically correct mixing rule for cubic equations of state. AIChE. J., 38: 671.