Abstract
Isobaric Vapor-Liquid-Liquid equilibrium data for the binary systems ethyl acetate + water, toluene +
water and the ternary system toluene + ethyl acetate + water were determined by a modified
equilibrium still, the still consisted of a boiling and a condensation sections supplied with mixers that
helped to correct the composition of the recycled condensed liquid and the boiling temperature readings
in the condensation and boiling sections respectively. The VLLE data where predicted and correlated
using the Peng-Robinson Equation of State in the vapor phase and one of the activity coefficient
models Wilson, NRTL, UNIQUAC and the UNIFAC in the liquid phase and also were correlated using
the Peng-Robinson Equation of State in both the vapor and liquid phases.
water and the ternary system toluene + ethyl acetate + water were determined by a modified
equilibrium still, the still consisted of a boiling and a condensation sections supplied with mixers that
helped to correct the composition of the recycled condensed liquid and the boiling temperature readings
in the condensation and boiling sections respectively. The VLLE data where predicted and correlated
using the Peng-Robinson Equation of State in the vapor phase and one of the activity coefficient
models Wilson, NRTL, UNIQUAC and the UNIFAC in the liquid phase and also were correlated using
the Peng-Robinson Equation of State in both the vapor and liquid phases.