Thermochimica Acta, Vol.268, 45-68, 1995
Representation of Phase-Equilibria Using a Modified Form of the Extended Uniquac Model
Binary infinite-dilution activity coefficients and LLE data for 14 systems (five aqueous systems, five alcohol + hydrocarbon systems, acetonitrile + n-hexane, and three nitroethane + hydrocarbon systems) are simultaneously correlated with a modification of the extended UNIQUAC model, which also reproduces well binary and ternary VLE data for mixtures containing methanol + +n-pentane bordering on liquid-liquid immiscibility.
Keywords:LIQUID-LIQUID EQUILIBRIA;EXCESS GIBBS ENERGY;VAPOR-LIQUID;TERNARY;COEFFICIENTS;PREDICTION;MIXTURES;EQUATION;METHANOL;SYSTEMS