Calculation of infinite dilution activity coefficients by the NRTL and UNIQUAC models
- 1 August 1990
- journal article
- research article
- Published by Wiley in The Canadian Journal of Chemical Engineering
- Vol. 68 (4) , 697-701
- https://doi.org/10.1002/cjce.5450680424
Abstract
No abstract availableKeywords
This publication has 27 references indexed in Scilit:
- Simultaneous correlation of excess gibbs energy and enthalpy of mixing by the UNIQUAC EquationThe Canadian Journal of Chemical Engineering, 1989
- Excess thermodynamic properties for the binary system 1,4-dioxane-acetonitrile at 40.degree.CJournal of Chemical & Engineering Data, 1988
- Vapor‐liquid equilibrium, excess gibbs energy and excess enthalpy of 1, 3 dioxolane‐methylcyclohexane at t = 313.15 kThe Canadian Journal of Chemical Engineering, 1988
- Sensitivity testing with the predictive thermodynamic models NRTL, UNIQUAC, ASOG and UNIFAC in multicomponent separations of methanol-acetone-chloroformChemical Engineering Science, 1988
- Vapor-liquid equilibrium measurements for the ethanol-acetone system at 372.7, 397.7, and 422.6 KJournal of Chemical & Engineering Data, 1987
- Selection of solvents for extractive distillation. A data bank for activity coefficients at infinite dilutionIndustrial & Engineering Chemistry Process Design and Development, 1985
- Excess Gibbs energies and excess volumes of 1-butanol-n-heptane and 2-methyl-1-propanol-n-heptane binary systemsJournal of Chemical & Engineering Data, 1984
- Excess Gibbs energies and excess volumes of 1-butanol-n-hexane and 2-methyl-1-propanol-n-hexane binary systemsJournal of Chemical & Engineering Data, 1982
- UNIFAC and infinite dilution activity coefficientsThe Canadian Journal of Chemical Engineering, 1982
- Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systemsAIChE Journal, 1975