A novel approach for determining vapor−liquid equilibrium (VLE) for polymer−diluent systems
is described. The concentration- and temperature-dependence of diluent−polymer Flory−Huggins
interaction parameter χij is first estimated from depression in polymer melting point as a function
of monomer (diluent) concentration. VLE for the polymer−diluent binary system is then obtained
using an activity coefficient model and equation of state model with Aspen Polymer Plus. The
technique is validated for the syndiotactic polystyrene−toluene and syndiotactic polystyrene−methyl ethyl ketone and is extended to polybutylene terephthalate − with various diluents such
as butanediol, tetrahydrofuran, isophorone, 1-methylnaphthalene, and benzonitrile, systems
hitherto not reported in the literature.