Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Separation of ethyl acetate and ethanol azeotrope mixture using dialkylphosphates-based ionic liquids as entrainers

Zhang, Zhigang, Wu, Kaifang, Zhang, Qinqin, Zhang, Tao, Zhang, Debiao, Yang, Ru, Li, Wenxiu
Fluid Phase Equilib. 2017, 454, 91-98
ABSTRACT
Isobaric vapor-liquid equilibrium (VLE) data for the ternary systems of ethyl acetate + ethanol + 1-ethyl-3-methylimidazolium diethylphosphate ([EMIM][DEP]), ethyl acetate + ethanol + 1-butyl-3-methylimidazolium diethylphosphate ([BMIM][DEP]) and ethyl acetate + ethanol + 1-butyl-3-methylimidazolium dibutylphosphate ([BMIM][DBP]) were measured at 101.3 kPa. The results showed that all the three ionic liquids (ILs) produced remarkable salting-out effect, leading to the increase of the relative volatility of ethyl acetate to ethanol. Hence, the azeotropic point of ethyl acetate and ethanol could be eliminated with the addition of a certain content of ILs. The separation effect of the three ILs follows the order of [EMIM][DEP] greater than [BMIM][DEP] greater than [BMIM][DBP]. Then, the experimental VLE data were well correlated with the nonrandom two-liquid (NRTL) model. Finally, the s-Profiles of solvents and ILs were used to analysis the micro-mechanism of the different separation performance of the three investigated ILs.
Compounds
# Formula Name
1 C4H8O2 ethyl acetate
2 C2H6O ethanol
3 C10H21N2O4P 1-ethyl-3-methylimidazolium diethyl phosphate
4 C16H33N2O4P 1-butyl-3-methylimidazolium dibutyl phosphate
5 C12H25N2O4P 1-butyl-3-methylimidazolium diethyl phosphate
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)
  • 16
  • POMD
  • 1
  • 2
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Chromatography
  • 16
  • POMD
  • 1
  • 2
  • 3
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 45
  • POMD
  • 1
  • 2
  • 3
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Chromatography
  • 45
  • POMD
  • 1
  • 2
  • 5
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 50
  • POMD
  • 1
  • 2
  • 5
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Chromatography
  • 50
  • POMD
  • 1
  • 2
  • 4
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 51
  • POMD
  • 1
  • 2
  • 4
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Gas
  • Gas
  • Liquid
  • Chromatography
  • 51