Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Ionic liquids as entrainers for the separation of the ethanol/water system

Tsanas, C.[Christos], Tzani, A.[Andromachi], Papadopoulos, A.[Achilleas], Detsi, A.[Anastasia], Voutsas, E.[Epaminondas]
Fluid Phase Equilib. 2014, 379, 148-156
ABSTRACT
Isobaric vapor-liquid equilibrium measurements of the ethanol/water binary mixture andethanol/water/ionic liquid ternary mixtures were performed using an ebuliometer at 101.3 and 66.6 kPa. The ionic liquids (ILs) synthesized and examined as entrainers for the ethanol/water azeotropic mixture were 1-butyl-3-methylimidazolium bromide ([BMIM][Br]) and 1-ethyl-3-methylimidazoliumbromide ([EMIM][Br]). For both ILs, the initial concentrations for the ternary mixtures were 5%, 10% and15% w/w. The entrainers were also tested for their recoverability and biodegradability. Analysis with1H NMR proved that the ionic liquids can be recycled and reused while their ability to biodegrade was found to be relatively low.Introduction of the entrainers to the ethanol/water system resulted in an increase of the relative volatility, due to the salting-out effect on ethanol, leading to the successful elimination of the azeotropic point. The effect on the relative volatility follows the order [EMIM][Br] greater than [BMIM][Br], which corresponds to the order of increasing affinity of water to the specific entrainers. Finally, the thermodynamic modeling of the ethanol/water/IL mixtures was investigated with the UNIQUAC and NRTL models. The results for both models were found to be in good agreement with the experimental data.
Compounds
# Formula Name
1 C2H6O ethanol
2 H2O water
3 C8H15BrN2 1-butyl-3-methylimidazolium bromide
4 C6H11BrN2 1-ethyl-3-methylimidazolium bromide
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
  • 2
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 7
  • POMD
  • 1
  • 2
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Gas
  • Liquid
  • Titration method
  • 7
  • POMD
  • 1
  • 2
  • 3
  • Boiling temperature at pressure P, K ; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Mass fraction - 3; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 36
  • POMD
  • 1
  • 2
  • 3
  • Mole fraction - 1 ; Gas
  • Pressure, kPa; Gas
  • Solvent: Mole fraction - 1; Liquid
  • Mass fraction - 3; Liquid
  • Gas
  • Liquid
  • Titration method
  • 36
  • POMD
  • 1
  • 2
  • 3
  • Mole fraction - 2 ; Gas
  • Pressure, kPa; Gas
  • Solvent: Mole fraction - 1; Liquid
  • Mass fraction - 3; Liquid
  • Gas
  • Liquid
  • Titration method
  • 36
  • POMD
  • 1
  • 2
  • 4
  • Boiling temperature at pressure P, K ; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 1; Liquid
  • Mass fraction - 4; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 36
  • POMD
  • 1
  • 2
  • 4
  • Mole fraction - 1 ; Gas
  • Pressure, kPa; Gas
  • Solvent: Mole fraction - 1; Liquid
  • Mass fraction - 4; Liquid
  • Gas
  • Liquid
  • Titration method
  • 36
  • POMD
  • 1
  • 2
  • 4
  • Mole fraction - 2 ; Gas
  • Pressure, kPa; Gas
  • Solvent: Mole fraction - 1; Liquid
  • Mass fraction - 4; Liquid
  • Gas
  • Liquid
  • Titration method
  • 36