Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

ABSTRACT

Vapour liquid equilibrium data in the two binary 2-propanol + 4-methyl-2-pentanone, and diisopropyl ether + 4-methyl-2-pentanone systems, and in the ternary 2-propanol + diisopropyl ether + 4-methyl-2-pentanone system are reported. The data were measured isothermally at 330.00 and 340.00K covering the pressure range 12 100 kPa. The binary vapour liquid equilibrium data were correlated using the Wilson, NRTL and Redlich Kister equations; resulting parameters were then used for calculation of phase behaviour in the ternary system and for subsequent comparison with experimental data.