Abstract
Isobaric vapor-liquid equilibrium data at 76Omm 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.
