Journal of Chemical and Engineering Data, Vol.41, No.4, 718-723, 1996
VLE Measurements of Binary-Mixtures of Methanol, Ethanol, 2-Methoxy-2-Methylpropane, and 2-Methoxy-2-Methylbutane at 101.32-kPa
Isobaric vapor-liquid equilibrium data for 2-methoxy-2-methylpropane + methanol, 2-methoxy-2-methylpropane + ethanol, methanol + 2-methoxy-2-methylbutane, ethanol + 2-methoxy-2-methylbutane, and 2-methoxy-2-methylpropane + 2-methoxy-2-methylbutane were determined at 101.32 kPa. Fredenslund et al.’s test confirmed the results to be thermodynamically consistent. The VLE data were satisfactorily correlated using the Wilson, NRTL, and UNIQUAC equations for liquid phase activity coefficients and adequately predicted using the ASOG, UNIFAC, UNIFAC-Dortmund, and UNIFAC-Lyngby group contribution methods.
Keywords:UNIFAC GROUP-CONTRIBUTION;VAPOR-LIQUID-EQUILIBRIA;TERT-BUTYL ETHER;PHASE-EQUILIBRIA;MODEL;PREDICTION