Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

ABSTRACT

Isobaric vapor liquid equilibrium (VLE) data for acetic acid +water, acetic acid +methyl ethyl ketone (MEK),MEK+ isopropyl acetate, acetic acid +MEK+water and acetic acid +MEK+ isopropyl acetate +water are measured at 101.33 kPa using a modified Rose cell. The nonideal behavior in vapor phase of binary systems measured in this work is analyzed through calculating fugacity coefficients since mixture containing acetic acid deviates from ideal behavior seriously in vapor phase due to the associating effect of acetic acid. Combined with Hayden O Connell (HOC) equation, the VLE data of the measured binary systems for acetic acid +water, acetic acid +MEK and MEK+ isopropyl acetate are correlated by the NRTL and UNIQUAC models. The NRTL model parameters obtained from correlating data of binary system are used to predict the VLE data of the ternary and quaternary systems, and the predicted values obtained in this way agree well with the experimental values.