Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Vapour pressure measurement for binary and ternary systems containing water methanol ethanol and an ionic liquid 1-ethyl-3-ethylimidazolium diethylphosphate

Jiang, X.-C.[Xiao-Chuan], Wang, J.-F.[Jun-Feng], Li, C.-X.[Chun-Xi], Wang, L.-M.[La-Mei], Wang, Z.-H.[Zi-Hao]
J. Chem. Thermodyn. 2007, 39, 6, 841-846
ABSTRACT
Vapour pressure data were measured for three binary systems containing water, methanol or ethanol with an ionic liquid (IL) 1-ethyl- 3-ethylimidazolium diethylphosphate([EEIM][DEP]) and for three ternary systems, i.e. (water + ethanol + [EEIM][DEP]), (water + methanol + [EEIM][DEP]), and (ethanol + methanol + [EEIM][DEP]), at varying temperature and IL-content ranging from mass fraction of 0.10 to 0.85 by a quasi-static method. The vapour pressure data of the binary systems were correlated by NRTL equation with average absolute relative deviation (ARD) within 0.0091. The binary NRTL parameters were used to predict the vapour pressure of the ternary systems (ethanol + water + [EEIM][DEP]), (water + methanol + [EEIM][DEP]), and (ethanol + methanol + [EEIM][DEP]) with an overall ARD of 0.037 and the maximum deviation of 0.1295. The results indicate that ionic liquid [EEIM][DEP] can give rise to a negative deviation from the Raoult s law for the solvents of water, methanol and ethanol, but to a varying degree leading to the variation of relative volatility of a solvent and even removal of azeotrope for (water + ethanol).
Compounds
# Formula Name
1 H2O water
2 CH4O methanol
3 C2H6O ethanol
4 C10H21N2O4P 1-ethyl-3-methylimidazolium diethyl phosphate
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
  • 1
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Twin ebulliometer
  • 31
  • POMD
  • 2
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Twin ebulliometer
  • 32
  • POMD
  • 3
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 3; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Twin ebulliometer
  • 30
  • POMD
  • 2
  • 1
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Twin ebulliometer
  • 32
  • POMD
  • 3
  • 1
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 3; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Twin ebulliometer
  • 32
  • POMD
  • 3
  • 2
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 3; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Twin ebulliometer
  • 31