Correlation of LLE (Liquid-Liquid Equilibria) of ternary systems by using Wilson equation has been studied and discussed. To extend Wilson equation for representing LLE, effective parameters should be added to the original Wilson equation to give larger molar excess Gibbs energy and more suitable function form. In this study, some ternary mixtures containing methanol such as heptane + methanol + benzene (Type 1 in LLE) have been examined. The role of additional parameters in calculating LLE has been quantitatively discussed.