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Measurements of Vapor-liquid Equilibria for Binary Systems Including Tetrahydropyran
Tetrahydropyran Vapor-liquid equilibria NRTL parameters ASOG group pair parameters
2009/8/4
The vapor-liquid equilibria (VLE) data of systems including tetrahydropyran (THP) are impotant, as tetrahydropyran is a useful reaction solvent and separation solvent, but are scarce in the literatur...
A GE/Equation of State Mixing Rule for Vapor-Liquid Equilibria
vapor-liquid equilibria equation of state mixing rule
2009/4/28
A new excess Gibbs free energy/equation of state type mixing 0rule was derived by removing the infinite pressure boundary condition imposed by Wong and Sandler. The mixing rule was extensively tested ...
Isobaric Vapor-Liquid Equilibria for 2-Methylphenol-2,6-Dimethylphenol-2,4,6-Trimethylphenol Ternary System
vapor-liquid equilibrium 2,6-dimethylphenol binary system ternary system
2009/4/21
Isobaric Vapor-Liquid Equilibria for 2-Methylphenol-2,6-Dimethylphenol-2,4,6-Trimethylphenol Ternary System.
The Performance of EOS Models in the Prediction of Vapor-Liquid Equilibria in Asymmetric Natural Gas Mixtures
equation of state natural gas vapor-liquid equilibria
2009/3/20
The aim of this work is to apply cubic equations of state (EOS) to vapor-liquid equilibria calculations of gas- heavy hydrocarbon systems, which are asymmetric in molecular size and are usually found ...
Vapor-Liquid Equilibria for Dimethyl Carbonate-n-Butyl Acetate Binary System at 101.325kPa
Dimethyl Carbonate-n-Butyl Vapor-Liquid Equilibria
2009/3/19
Vapor-Liquid Equilibria for Dimethyl Carbonate-n-Butyl Acetate Binary System at 101.325kPa。