Vapor−Liquid Equilibrium of the Ternary System Ethyl Acetate + Hexane + Acetone at 101.32 kPa

Abstract

Experimental isobaric vapor−liquid equilibrium data at 101.32 kPa for the ternary system ethyl acetate + hexane + acetone and for its constituent binary systems are reported. These data were found to be thermodynamically consistent and were satisfactorily correlated with the Wilson, NRTL, and UNIQUAC equations. They were also compared with predictions of the ASOG and UNIFAC group contribution methods.