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

Vapor-Liquid Equilibria of the Carbon Dioxide + Acetone System at Pressures from (2.36 to 11.77) MPa and Temperatures from (333.15 to 393.15) K

Han, F.[Fang], Xue, Y.[Yuan], Tian, Y.[Yiling], Zhao, X.[Xuefeng], Chen, L.[Li]
J. Chem. Eng. Data 2005, 50, 1, 36-39
ABSTRACT
High-pressure phase equilibrium data p, T, x, F, and Vm for the binary carbon dioxide + acetone system were measured at several temperatures (333.15, 353.15, 373.15, and 393.15) K and pressures from (2.36 to 11.77) MPa. The experimental data at 333.15 K are in good agreement with literature data, and the experimental results are correlated by the Peng-Robinson equation.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 C3H6O acetone
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
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • CCELL:UFactor:8
  • 30