Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Binary vapor liquid equilibrium of methyl glycolate and ethylene glycol

Sun, L., Fu, J. -Y.[Jin-Yan], Li, W.[Wei], Xiao, W. D.[Wen-De]
Fluid Phase Equilib. 2006, 250, 1-2, 33-36
ABSTRACT
Vapor pressure of methyl glycolate and the binary isothermal vapor liquid equilibrium of ethylene glycol and methyl glycolate were measured by using static method. The experimental data was correlated with theWilson and NRTL activity coefficient models. Good agreement between the experimental data and model is achieved.
Compounds
# Formula Name
1 C2H6O2 1,2-ethanediol
2 C3H6O3 methyl hydroxyethanoate
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
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • CCELL:UFactor:16
  • 7
  • POMD
  • 2
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Liquid
  • Gas
  • CCELL:UFactor:8
  • 40