A method for incorporating excess Gibbs energy models in equations of state

Fluid Phase Equilibria

Volumn 60, Issue 1-2, 1990, Pages 47-58

  Michelsen, Michael L ^a  

^a TECHNICAL UNIVERSITY OF DENMARK   (Denmark)

Author keywords

[No Author keywords available]

Indexed keywords

MIXTURES--PHASE EQUILIBRIA;

EXCESS GIBBS ENERGY MODELS; MIXING RULES; VAPOR-LIQUID EQUILIBRIUM;

EQUATIONS OF STATE;

EID: 0025499797     PISSN: 03783812     EISSN: None     Source Type: Journal    
DOI: 10.1016/0378-3812(90)85042-9     Document Type: Article

References (12)

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2. Thermodynamic properties of methanol-benzene mixtures at elevated temperatures
3. Prediction of gas solubility and VLE by group contribution
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5. DECHEMA Chemistry Data Series
6. Phase equilibria of the acetone—methanol—water system from 100°C into the critical region
7. A new group-contribution equation of state for vapour—liquid equilibria
8. Combined excess free energy models and equations of state. 4th CODATA Symposium, September 4–6, 1989. Gradisca d'Isonzo, Italy
9. New mixing rules in simple equations of state for representing vapor—liquid equilibria of strongly non-ideal mixtures
10. A note on the derivation of mixing rules from excess Gibbs energy models
11. A new two-constant equation of state
12. Equilibrium constants from a modified Redlich-Kwong equation of state