Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Vapor pressure measurement for binary and ternary systems containing a phosphoric ionic liquid

Zhao, J., Jiang, K.-C.[Kiao-Chuan], Li, C.-X.[Chun-Xi], Wang, Z.-H.[Zi-Hao]
Fluid Phase Equilib. 2006, 247, 1-2, 190-198
ABSTRACT
Vapor pressure data were measured for nine binary systems containing water, methanol or ethanol with the ionic liquids 1-methyl-3-methylimidazolium dimethylphosphate ([MMIM][DMP]), 1-ethyl-3-methylimidazolium diethylphosphate ([EMIM][DEP]) and 1-butyl-3-methylimidazolium dibutylphosphate ([BMIM][DBP]) and one ternary system ethanol?water?[MMIM][DMP] at varying temperature and ionic liquid mass percent ranging from 10% to 70% by a quasi-static method. The vapor pressure data of the binary systems were correlated by NRTL model with overall average absolute relative deviation (ARD) of 0.89% and a maximum ARD within 2%. Based on the vapor pressure depression of binary systems interpolated at ionic liquid mole fraction 0.05 in the temperature range from 280 to 370 K, it is shown that the effect of ionic liquid on the vapor pressure lowering follows the order [MMIM][DMP] > [EMIM][DEP] > [BMIM][DBP] for water, and [BMIM][DBP] > [EMIM][DEP] > [MMIM][DMP] for methanol and ethanol, suggesting that the ?ionic? characteristic of the ionic liquid dominates in water, while the ?molecule? characteristic prevails in organic solvent. The binary NRTL parameters were used to predict the vapor pressure of the ternary system ethanol?water?[MMIM][DMP] with an ARD of 2.8% and the maximum relative deviation of -5.43%.
Compounds
# Formula Name
1 C7H15N2O4P 1,3-dimethylimidazolium dimethylphosphate
2 C10H21N2O4P 1-ethyl-3-methylimidazolium diethyl phosphate
3 C16H33N2O4P 1-butyl-3-methylimidazolium dibutyl phosphate
4 C2H6O ethanol
5 CH4O methanol
6 H2O water
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
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 11
  • POMD
  • 6
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 38
  • POMD
  • 5
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 38
  • POMD
  • 4
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 38
  • POMD
  • 6
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 38
  • POMD
  • 5
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 38
  • POMD
  • 4
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 38
  • POMD
  • 6
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 3; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 38
  • POMD
  • 5
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 3; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 38
  • POMD
  • 4
  • 3
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 3; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 38
  • POMD
  • 4
  • 6
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mass fraction - 4; Liquid
  • Mass fraction - 6; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 32