Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Vapor-Liquid Equilibrium for Tetrahydrofuran + Methanol + Tetrafluoroborate-based ionic liquids at 101.3 kPa

Li, Q.[Qunsheng], Liu, P.[Panpan], Cao, L.[Ling], Wen-jun, F.[Fang], Zhang, S.[Shuang], Wang, B.[Baohua]
Fluid Phase Equilib. 2013, 360, 439-444
ABSTRACT
The vapor-liquid equilibrium (VLE) data for the ternary systems of tetrahydrofuran (THF) (1) + methanol (2) + 1-ethyl-3-methylimidazolium tetrafluoroborate ([EMIM][BF4]) (3) and THF (1) + methanol (2) + 1-butyl-3-methylimidazolium tetrafluoroborate ([BMIM][BF4]) (3) are measured at 101.3 kPa with a modified Othmer still. The ionic liquids (ILs) give rise to the relative volatility of THF to methanol. [EMIM][BF4] has a stronger effect on the enhancement of the relative volatility than [BMIM][BF4]. [EMIM][BF4] even eliminates the azeotropic point when its mole fraction is up to 0.20, whereas [BMIM][BF4] pulls down the azeotropic point. The effect of two ILs on the VLE for THF + methanol system is discussed. The NRTL model proposed by Renon and Prausnitz reproduces the experimental values well.
Compounds
# Formula Name
1 C4H8O tetrahydrofuran
2 CH4O methanol
3 C6H11BF4N2 1-ethyl-3-methylimidazolium tetrafluoroborate
4 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
  • 2
  • 1
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 15
  • POMD
  • 2
  • 1
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • Chromatography
  • 15
  • POMD
  • 2
  • 1
  • Azeotropic temperature, K ; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 1
  • POMD
  • 2
  • 1
  • Azeotropic composition: mole fraction - 1 ; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • By X=Y
  • 1
  • POMD
  • 2
  • 1
  • 3
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 3; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 27
  • POMD
  • 2
  • 1
  • 3
  • Mole fraction - 1 ; Gas
  • Mole fraction - 3; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Chromatography
  • 27
  • POMD
  • 2
  • 1
  • 3
  • Mole fraction - 2 ; Gas
  • Mole fraction - 3; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Chromatography
  • 27
  • POMD
  • 2
  • 1
  • 4
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 4; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 27
  • POMD
  • 2
  • 1
  • 4
  • Mole fraction - 1 ; Gas
  • Mole fraction - 4; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Chromatography
  • 27
  • POMD
  • 2
  • 1
  • 4
  • Mole fraction - 2 ; Gas
  • Mole fraction - 4; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Chromatography
  • 27