Vapor-liquid equilibrium data for the ternary systems: Methyl acetate-2-prop anol-benzene and methyl acetate-chloroform-benzene

Abstract

Isobaric vapor-liquid equilibrium data at 760mm of Hg were determined for the ternary methyl acetate-2-propanol-benzene system and isothermal equilibrium data at 50°C were obtained for the ternary system methyl acetate-chloroform-benzene and for its binary systems, methyl acetate-chloroform, methyl acetate-benzene, and chloroform-benzene, using a Jones still. The Wilson and NRTL equations were successfully applied for the correlation of the liquid-phase activity coefficient and for the prediction of ternary equilibrium data. © 1970, The Society of Chemical Engineers, Japan. All rights reserved.