Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Solubilities of several non-polar gases in mixtures water + 2,2,2-trifluoroethanol at 298.15 K and 101.33 kPa

Mainar, A. M.[Ana M.], Martinez-Lopez, J. F.[Jose F.], Langa, E.[Elisa], Pardo, J. I.[Juan I.], Urieta, J. S.[Jose S.]
Fluid Phase Equilib. 2012, 314, 161
ABSTRACT
Solubilities of nine nonpolar gases (H2, N2, O2, CH4, C2H6, C2H4, CF4, SF6, and CO2) in mixtures of water + 2,2,2-trifluoroethanol (TFE) at 298.15 K and 101.33 kPa partial pressure of gas are reported. A polynomial dependence of the solubilities on the molar fraction of the binary liquid mixture is found. The Henry's constants at the vapour pressure of water, the standard changes in the Gibbs energy for the solution process and for the solvation process, and the so-called excess Henry's constant are calculated. Gibbs energies for the solution process and excess Henry's constants have been calculated using the Scaled Particle Theory (SPT).
Compounds
# Formula Name
1 H2O water
2 C2H3F3O 2,2,2-trifluoroethanol
3 H2 hydrogen
4 N2 nitrogen
5 O2 oxygen
6 CH4 methane
7 C2H6 ethane
8 C2H4 ethene
9 CF4 tetrafluoromethane
10 F6S sulfur hexafluoride
11 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
  • 3
  • 1
  • Mole fraction - 3 ; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Gas
  • Liquid
  • Gas
  • Saturation method
  • 9
  • POMD
  • 2
  • 4
  • 1
  • Mole fraction - 4 ; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Saturation method
  • 9
  • POMD
  • 2
  • 1
  • 5
  • Mole fraction - 5 ; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Gas
  • Liquid
  • Gas
  • Saturation method
  • 9
  • POMD
  • 6
  • 2
  • 1
  • Mole fraction - 6 ; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Gas
  • Liquid
  • Gas
  • Saturation method
  • 9
  • POMD
  • 7
  • 2
  • 1
  • Mole fraction - 7 ; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Gas
  • Liquid
  • Gas
  • Saturation method
  • 9
  • POMD
  • 8
  • 2
  • 1
  • Mole fraction - 8 ; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Gas
  • Liquid
  • Gas
  • Saturation method
  • 9
  • POMD
  • 9
  • 2
  • 1
  • Mole fraction - 9 ; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Gas
  • Liquid
  • Gas
  • Saturation method
  • 9
  • POMD
  • 2
  • 10
  • 1
  • Mole fraction - 10 ; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Gas
  • Liquid
  • Gas
  • Saturation method
  • 9
  • POMD
  • 2
  • 11
  • 1
  • Mole fraction - 11 ; Liquid
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Saturation method
  • 9