Thermodynamics Research Center / ThermoML | Thermochimica Acta

Thermodynamic behavior of binary mixtures CnMpyNTf2 ionic liquids with primary and secondary alcohols

Calvar, N., Gomez, E., Dominguez, A., Macedo, E. A.
Thermochim. Acta 2012, 549, 49-56
ABSTRACT
In this paper, the osmotic and activity coefficients and vapor pressures of the binary mixtures containing the ionic liquids 1-ethyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide, C2MpyNTf2, and 1-methyl-3-propylpyridinium bis(trifluoromethylsulfonyl)imide, C3MpyNTf2, with 1-propanol, or 2-propanol and the ionic liquid 1-butyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide, C4MpyNTf2, with 1-propanol or 2-propanol or 1-butanol or 2-butanol were determined at T = 323.15 K using the vapor pressure osmometry technique. The influence of the structure of the alcohol and of the ionic liquid on both coefficients and vapor pressures is discussed and a comparison with literature data on binary mixtures containing ionic liquids with different cations and anion is also performed. Besides, the results have been interpreted in terms of solute solvent and ion ion interactions. The experimental osmotic coefficients were correlated using the Extended Pitzer model of Archer and the Modified Non-Random Two Liquids model obtaining standard deviations lower than 0.059 and 0.102 respectively, and the mean molal activity coefficients and the excess Gibbs free energy for the studied mixtures were calculated.
Compounds
# Formula Name
1 C10H12F6N2O4S2 1-ethyl-3-methylpyridinium bis((trifluoromethyl)sulfonyl)amide
2 C11H14F6N2O4S2 3-methyl-1-propylpyridinium bis(trifluoromethylsulfonyl)imide
3 C3H8O propan-1-ol
4 C3H8O propan-2-ol
5 C12H16F6N2O4S2 1-butyl-3-methylpyridinium 1,1,1-trifluoro-N-[(trifluoromethyl)sulfonyl]methanesulfonamide
6 C4H10O butan-1-ol
7 C4H10O butan-2-ol
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
  • 3
  • 1
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 14
  • POMD
  • 3
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 15
  • POMD
  • 3
  • 5
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 5; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 14
  • POMD
  • 4
  • 1
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 14
  • POMD
  • 4
  • 2
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 14
  • POMD
  • 4
  • 5
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 5; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 14
  • POMD
  • 6
  • 5
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 5; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 14
  • POMD
  • 7
  • 5
  • Osmotic coefficient ; Liquid
  • Molality, mol/kg - 5; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 14