Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Separation of the isopropanol-water azeotropic mixture using ionic liquids

Boli, Elenitsa, Dimou, Elpianna, Voutsas, Epaminondas
Fluid Phase Equilib. 2018, 456, 77-83
ABSTRACT
Vapor-liquid equilibrium (VLE) measurements of the isopropanol-water-ionic liquid ternary mixtures were performed using an ebuliometer at 101.3 kPa. The ionic liquids (ILs) synthesized and examined as entrainers for breaking the azeotrope of the isopropanol-water mixture are: 2-hydroxyethylammonium formate (2HEAF), 2-hydroxyethylammonium acetate (2HEAA) and 2-hydroxyethylammonium butyrate (2HEAB). Three initial IL (entrainer) concentrations in the feed solution were examined in the VLE experiments: at approximately 9%, 14.5% and 19.2% w/w. It is shown that the introduction of the entrainers to the isopropanol-water system results in an increase of the relative volatility leading to the successful elimination of the azeotropic point. The relative volatilities decrease with increasing the alkyl chain length of the anion of the IL, following the order: 2HEAB less than 2HEAA less than 2HEAF. Dynamic viscosities of the ionic liquids were measured in the temperature range from (293.15 to 363.15) K. Finally, thermodynamic modeling of the isopropanol-water-IL mixtures was performed with the UNIQUAC and NRTL models, and the results for both models were found to be in good agreement with the experimental data.
Compounds
# Formula Name
1 C3H8O propan-2-ol
2 H2O water
3 C3H9NO3 2-hydroxyethylammonium formate
4 C4H11NO3 2-hydroxyethylammonium acetate
5 C6H15NO3 2-hydroxy ethylammonium butanoate
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
  • 3
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • OTHER:UFactor:12:sMethod:Brookfield Digital Viscometer
  • 15
  • POMD
  • 4
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • OTHER:UFactor:6:sMethod:Brookfield Digital Viscometer
  • 15
  • POMD
  • 5
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • OTHER:UFactor:6:sMethod:Brookfield Digital Viscometer
  • 15
  • POMD
  • 1
  • 2
  • 3
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • ebulliometer
  • 24
  • POMD
  • 1
  • 2
  • 3
  • Mole fraction - 1 ; Gas
  • Temperature, K; Gas
  • Mole fraction - 3; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Titration method
  • 24
  • POMD
  • 1
  • 2
  • 4
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 4; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • ebulliometer
  • 22
  • POMD
  • 1
  • 2
  • 4
  • Mole fraction - 1 ; Gas
  • Temperature, K; Gas
  • Mole fraction - 4; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Titration method
  • 22
  • POMD
  • 1
  • 2
  • 5
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 5; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • ebulliometer
  • 24
  • POMD
  • 1
  • 2
  • 5
  • Mole fraction - 1 ; Gas
  • Temperature, K; Gas
  • Mole fraction - 5; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Titration method
  • 24