Simultaneous representation of excess enthalpy and vapor—liquid equilibrium data by the NRTL and UNIQUAC models-Reference-Cited by-同舟云学术

Simultaneous representation of excess enthalpy and vapor—liquid equilibrium data by the NRTL and UNIQUAC models

Published:1991-01 Issue: Volume:65 Page:111-133
ISSN:0378-3812
Container-title:Fluid Phase Equilibria
language:en
Short-container-title:Fluid Phase Equilibria

Author:

Demirel Yaşsar,Gecegörmez Hatice

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering

Reference49 articles.

1. Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systems;Abrams;AIChE J.,1975

2. Application of the UNIQUAC equation to calculation of multicomponent phase equilibria 1. Vapour—liquid equilbria;Anderson;Ind. Eng. Chem. Proc. Des. Dev.,1978

3. Excess energies and excess volumes of 1-butanol—n-heptane and 2-methyl-1-propanol—n-heptane binary systems;Berro;J. Chem. Eng. Data,1984

4. Excess Gibbs energies and excess volumes of 1-butanol—n-hexane and 1-methyl-1-propanol—n-hexane binary systems;Berro;Ind. Eng. Chem. Process Des. Dev.,1982

5. Sensitivity testing with the predictive thermodynamic models NRTL, UNIQUAC, ASOG and UNIFAC in multicomponent separations of methanol—acetone—chloroform;Cairns;Chem. Eng. Sci.,1988

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