Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Measurements of isothermal vapor-liquid equilibrium of binary methanol/dimethyl carbonate system under pressure

Yunhai, S.[Shi], Honglai, L.[Liu], Kun, W.[Wang], Wende, X.[Xiao], Ying, H.[Hu]
Fluid Phase Equilib. 2005, 234, 1-2, 1-10
ABSTRACT
Compounds
# Formula Name
1 C3H6O3 dimethyl carbonate
2 CH4O methanol
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
  • 5
  • POMD
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • CCELL:UFactor:2
  • 5
  • POMD
  • 2
  • 1
  • Azeotropic pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • PX:UFactor:3
  • 5
  • POMD
  • 2
  • 1
  • Azeotropic composition: mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • TPX:UFactor:16
  • 5
  • POMD
  • 2
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Gas
  • Liquid
  • CCELL:UFactor:2
  • 66