Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters

Chaudhari, S. K., Salavera, D., Esteve, X., Coronas, A.
Fluid Phase Equilib. 2008, 271, 1-2, 28-33
ABSTRACT
The vapour liquid equilibria (p, T, x) of a 1,1,1,2-tetrafluoroethane + ethylene-glycol dimethylether mixture was measured using the static method in the temperature range (283.15 353.15)K in steps of 10 K. The vapour liquid equilibrium data were correlated by the temperature-dependent five-parameter nonrandom two-liquid (NRTL) equation. The data obtained in this experiment together with our previous experimental data for the binary system1,1,1,2-tetrafluoroethane + triethylene-glycol dimethyletherwere used to calculate the UNIFAC interaction parameters for the CF3 and CH2F groups with the CH3, CH2, CH3O and CH2O groups. The resulting interaction parameters were used to predict the vapour pressures of the various mixtures studied in the literature.
Compounds
# Formula Name
1 C2H2F4 1,1,1,2-tetrafluoroethane
2 C4H10O2 1,2-dimethoxyethane
Datasets
The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type Compound-# Property Variable Constraint Phase Method #Points
  • POMD
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • CCELL:UFactor:2
  • 8
  • POMD
  • 2
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • CCELL:UFactor:2
  • 88