Journal of Chemical and Engineering Data, Vol.40, No.2, 515-518, 1995
Isobaric Vapor-Liquid-Equilibria of Methanol Plus Hexyl Acetate and Ethanol Plus Hexy Acetate
Vapor-liquid equilibria of methanol + hexyl acetate and ethanol + hexyl acetate mixtures were determined at 101.32 kPa. The data were checked for thermodynamic consistency using Fredenslund’s test, correlated using Wilson, NRTL, and UNIQUAC equations for the liquid phase activity coefficients, and compared with the predictions of the group contribution methods UNIFAC and ASOG.
Keywords:UNIFAC GROUP CONTRIBUTION;COEFFICIENTS