Thermochimica Acta, Vol.228, 283-289, 1993
Isobaric Vapor-Liquid-Equilibria in the Mixtures of 1-Heptyne+butanal, 1-Octyne+3-Octyne, +ethylbenzene and +dibutyl Ether, 2-Octyne+dibutyl Ether and +1-Butanol, and 3-Octyne+1-Octene
For seven binary systems containing isomeric alkynes, the isobaric variations of the boiling temperature with liquid-phase composition were determined using a semi-micro ebulliometer over the entire composition range. The experimental data were used to fit the adjustable parameters in the Redlich-Kister and Wilson equations. The new UNIFAC interaction parameters were determined separately for the terminal and internal triple-bond groups.