Vapor-liquid equilibria at 1 atm for binary and ternary systems composed of benzene, toluene, and m-xylene

The vapor-liquid equilibrium data for the binary and ternary systems composed of benzene, toluene, and m-xylene at the isobaric condition of 1 atm are presented. The experimental data of the binary systems were used to calculate the binary parameters of the Wilson equation. The calculated vapor-phase compositions and boiling points of the three binary and of the ternary systems agree well with the experimental data