Vapor-liquid equilibrium was measured for the binary systems methanol + o-xylene, ethanol + o-xylene, methyl acetate + o-xylene and ethyl acetate + o-xylene, and for the multicomponent mixtures methanol + methyl acetate + o-xylene, ethanol + ethyl acetate + o-xylene, and methanol + ethanol + methyl acetate + ethyl acetate + o-xylene at 101.3 kPa. The Wilson and Wan Laar models were compared with the UNIFAC method. Results show that the correlation was satisfactory.