Vapor-liquid equilibria for binary and ternary systems composed of acetone, 2-propanol, and 1-propanol

The vapor-liquid equilibrium data for the binary and ternary systems composed of acetone, 2-propanol, and 1-propanol at the isobaric condition of 760 mmHg are presented. The experimental data of the binary systems were used to calculate the binary parameters of the Wilson equation. These parameters have been used to calculate vapor-phase compositions and boiling points of related binary and ternary systems. Calculated vapor-phase compositions and boiling points have been obtained very close to the experimental data for each system investigated.