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

Fluid Phase Behavior of Nitrogen + Acetone and Oxygen + Acetone by Molecular Simulation, Experiment and the Peng Robinson Equation of State

Windmann, T.[Thorsten], Linnemann, M.[Matthias], Vrabec, J.[Jadran]
J. Chem. Eng. Data 2014, 59, 1, 28-38
ABSTRACT
Vapor liquid equilibria (VLE) of the binary mixtures nitrogen + acetone and oxygen + acetone are studied by molecular simulation and experiment. A force field model for pure acetone (CH3 (C-O) CH3) is developed, validated, and then compared with four molecular models from the literature. The unlike dispersive interaction between nitrogen and acetone as well as oxygen and acetone is adjusted. On the basis of these mixture models, the VLE of nitrogen + acetone and oxygen + acetone is determined by molecular simulation and validated on the basis of experimental data. To extend the experimental database, a gas solubility apparatus is constructed and the saturated liquid line of nitrogen + acetone is measured at the three isotherms 400 K, 450 K, and 480 K up to a maximum pressure of 41 MPa. Finally, the results from simulation and experiment are used to parametrize the Peng Robinson EOS for nitrogen + acetone with the Huron-Vidal mixing rule.
Compounds
# Formula Name
1 N2 nitrogen
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
  • Ebulliometric method (Recirculating still)
  • 24