Thermodynamic modeling of vapor-liquid equilibrium of binary systems ionic liquid + supercritical {CO2 or CHF3} and ionic liquid + hydrocarbons using Peng-Robinson equation of state

Journal of the Chinese Institute of Chemical Engineers

Volumn 39, Issue 4, 2008, Pages 353-360

  Álvarez, Víctor H ^a   Aznar, Martín ^a  

^a UNIVERSITY OF CAMPINAS   (Brazil)

Author keywords

Equation of state; Ionic liquids; Vapor liquid equilibrium

Indexed keywords

BINARY MIXTURES; BINS; CARBON DIOXIDE; EQUATIONS OF STATE; FREE ENERGY; GENETIC ALGORITHMS; GIBBS FREE ENERGY; IONIC LIQUIDS; LIQUIDS; MIXING; PHASE EQUILIBRIA; SYSTEMS (METALLURGICAL); VAN DER WAALS FORCES;

ACTIVITY COEFFICIENT MODEL; BINARY INTERACTION PARAMETER; EQUATION OF STATE; EXCESS GIBBS FREE ENERGY; FUGACITY CO-EFFICIENTS; PENG-ROBINSON EQUATION OF STATE; THERMODYNAMIC MODEL; WONG-SANDLER MIXING RULES;

EQUATIONS OF STATE OF LIQUIDS;

EID: 84962460686     PISSN: 03681653     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.jcice.2008.02.007     Document Type: Article

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