Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

Determination of Vapor Liquid Equilibria of the Binary System of Sub- and Supercritical CO2 and Diethyl Fumarate

Cucek, D.[Denis], Knez, Z.[Zeljko], Skerget, M.[Mojca]
J. Chem. Eng. Data 2014, 59, 5, 1528-1532
ABSTRACT
High-pressure liquid vapor phase equilibrium data (P T x y) for the binary mixture of the ester diethyl fumarate with CO2 have been measured at temperatures of (373.2, 398.2, 423.2, and 453.2) K over the pressure range from (2.5 to 23) MPa using a static-analytic method. The results show that the molar fraction of CO2 in the liquid phase increases with increasing pressure at the studied temperatures and decreases with increasing temperature at constant pressure, while the composition of the light phase remains more or less unchanged. The experimental results were correlated using the Peng Robinson equation of state in combination with one fluid mixing rule with two adjustable parameters, and the binary interaction parameters were calculated as functions of temperature. Overall, the absolute average relative deviations of the model from the data obtained for the light and heavy phases ranged from (8 to 10) % and (4 to 12) %, respectively.
Compounds
# Formula Name
1 C8H12O4 diethyl fumarate
2 CO2 carbon dioxide
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
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:24
  • 31
  • POMD
  • 2
  • 1
  • Mole fraction - 2 ; Gas
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Gas
  • Liquid
  • Density calibration data
  • 31