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

Isobaric Vapor-Liquid Equilibria for Three Ternary Systems: Water + 2-Propanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate, Water + 1-Propanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate, and Water + 1-Propanol + 1-Butyl-3-methylimidazolium Tetrafluoroborate

Zhang, L.[Lianzhong], Han, J.[Jianzhi], Wang, R.[Rongjie], Qiu, X.[Xingying], Ji, J.[Jianbing]
J. Chem. Eng. Data 2007, 52, 4, 1401-1407
ABSTRACT
Isobaric vapor-liquid equilibrium (VLE) data were measured for three ternary systems containing ionic liquids (ILs): water + 2-propanol + 1-ethyl-3-methylimidazolium tetrafluoroborate ([emim][BF4]), water + 1-propanol + [emim][BF4], and water + 1-propanol + 1-butyl-3-methylimidazolium tetrafluoroborate ([bmim][BF4]). The measurements were performed at P ) 100 kPa and at several constant IL mass fractions. Activity coefficients of the volatile components were obtained without the need of a thermodynamic model of the liquid phase. The effect of the ILs on the relative volatility of the volatile components was depicted separately by their effect on the activity coefficients. Results of the activity coefficients showed that [emim]+ has a stronger interaction with water than [bmim]+; however, it has a weaker interaction with 1-propanol or 2-propanol. Boiling temperature data were also measured at 100 kPa for the six binary systems containing ILs. Ternary VLE data were also calculated from binary NRTL parameters, which were obtained from correlations of the binary boiling temperature data.
Compounds
# Formula Name
1 H2O water
2 C3H8O propan-1-ol
3 C3H8O propan-2-ol
4 C6H11BF4N2 1-ethyl-3-methylimidazolium tetrafluoroborate
5 C8H15BF4N2 1-butyl-3-methylimidazolium tetrafluoroborate
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
  • 5
  • Boiling temperature at pressure P, K ; Liquid
  • Mass fraction - 5; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 7
  • POMD
  • 1
  • 4
  • Boiling temperature at pressure P, K ; Liquid
  • Mass fraction - 4; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 9
  • POMD
  • 3
  • 5
  • Boiling temperature at pressure P, K ; Liquid
  • Mass fraction - 5; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 15
  • POMD
  • 3
  • 4
  • Boiling temperature at pressure P, K ; Liquid
  • Mass fraction - 4; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 7
  • POMD
  • 2
  • 5
  • Boiling temperature at pressure P, K ; Liquid
  • Mass fraction - 5; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 8
  • POMD
  • 2
  • 4
  • Boiling temperature at pressure P, K ; Liquid
  • Mass fraction - 4; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 5
  • POMD
  • 3
  • 1
  • 4
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 53
  • POMD
  • 3
  • 1
  • 4
  • Mole fraction - 3 ; Gas
  • Mole fraction - 1; Liquid
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • CHROM:UFactor:4
  • 53
  • POMD
  • 2
  • 1
  • 4
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 22
  • POMD
  • 2
  • 1
  • 4
  • Mole fraction - 2 ; Gas
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • CHROM:UFactor:4
  • 22
  • POMD
  • 2
  • 1
  • 5
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:8
  • 35
  • POMD
  • 2
  • 1
  • 5
  • Mole fraction - 2 ; Gas
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • CHROM:UFactor:4
  • 35