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

Vapor Pressure Measurement and Prediction for Ethanol + Methanol and Ethanol + Water Systems Containing Ionic Liquids

Zhao, J.[Jin], Li, C.-X.[Chun-Xi], Wang, Z.-H.[Zi-Hao]
J. Chem. Eng. Data 2006, 51, 5, 1755-1760
ABSTRACT
Vapor pressure data for ternary systems ethanol + methanol + [MMIM][DMP] (1-methyl-3-methylimidazolium dimethyl phosphate), ethanol + methanol + [EMIM][DEP] (1-ethyl-3-methylimidazolium diethyl phosphate), ethanol + methanol + [BMIM][DBP] (1-butyl-3-methyl imidazolium dibutyl phosphate), and ethanol + water + [MMIM][DMP] were measured at ionic liquid (IL) mass fraction of 50 % by a quasi-static method. The vapor pressure data were correlated with the NRTL model for nonelectrolyte solution, and the average absolute relative deviations of vapor pressure for the above systems were 0.55 %, 0.42 %, 0.67 %, and 1.68 %, respectively. On the basis of the predicted isothermal vapor-liquid equilibrium data for the ethanol + methanol and ethanol + water systems at 320 K and ionic liquid mass fraction of 50 %, it is found that all ILs show salting-out effect for ethanol. The salting-out effect follows the order [EMIM][DEP] greater than [MMIM][DMP] greater than [BMIM][DBP] for the ethanol + methanol system. Moreover, the azeotropic phenomenon in the ethanol + water system can be completely removed. Furthermore, the ethanol component in the ethanol + methanol system is converted from a heavy component to a light one due to the stronger affinity between methanol and IL involved, which is helpful for the separation of methanol and water from ethanol.
Compounds
# Formula Name
1 CH4O methanol
2 C2H6O ethanol
3 H2O water
4 C10H21N2O4P 1-ethyl-3-methylimidazolium diethyl phosphate
5 C16H33N2O4P 1-butyl-3-methylimidazolium dibutyl phosphate
6 C7H15N2O4P 1,3-dimethylimidazolium dimethylphosphate
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
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 1
  • Refractive index (Na D-line) ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Standard Abbe refractometry
  • 1
  • POMD
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:4
  • 1
  • POMD
  • 2
  • Refractive index (Na D-line) ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Standard Abbe refractometry
  • 1
  • POMD
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Twin ebulliometer
  • 11
  • POMD
  • 2
  • 1
  • 6
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:2
  • 40
  • POMD
  • 2
  • 1
  • 4
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:2
  • 40
  • POMD
  • 2
  • 1
  • 5
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:2
  • 39
  • POMD
  • 2
  • 3
  • 6
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 2; Liquid
  • Mole fraction - 3; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:2
  • 48