Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Excess molar enthalpies for binary carbon dioxide + diethyl carbonate system at 298.15 - 308.15K and 5.0 - 6.5MPa

Matsuda, H.[Hiroyuki], Yoshii, S.[Shigetaka], Nagashima, A.[Akinori], Kurihara, K.[Kiyofumi], Ochi, K.[Kenji]
Fluid Phase Equilib. 2005, 236, 1-2, 146-155
ABSTRACT
The excess molar enthalpies of the carbon dioxide + diethyl carbonate system were determined using a flow-type isothermal microcalorimeter at temperatures from 298.15 to 308.15K and pressures from 5.0 to 6.5MPa. Mixtures shows strong exothermic behavior in these regions. In addition, a strong pressure dependency of the excess molar enthalpies was observed, and the excess molar enthalpy values decreased with increasing pressure. The experimental results were correlated using a composition-dependent equation and the Peng Robinson equation of state with the conventional mixing rule. Finally, the prediction of excess molar enthalpies using three mixing rules (MHV1, MHV2, and Wong Sandler) was also tested on the basis of the vapor liquid equilibrium data.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 C5H10O3 diethyl carbonate
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
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Flow calorimetry
  • 160