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

Vapor-Liquid Equilibria for R1234ze(E) and Three Imidazolium-Based Ionic Liquids as Working Pairs in Absorption-Refrigeration Cycle

Sun, Yanjun, Zhang, Yao, Di, Gaolei, Wang, Xiaopo, Prausnitz, John M., Jin, Liwen
J. Chem. Eng. Data 2018, 63, 8, 3053-3060
ABSTRACT
The performance of absorption-refrigeration cycle mainly depends on the thermodynamic properties of a working-fluid pair composed of a refrigerant and an absorbent. Particularly important is the solubility of the vaporized refrigerant in the absorbent. Using an isochoric saturation method, solubilities were measured for trans-1,3,3,3-tetrafluoropropene (R1234ze(E)) in 1-butyl-3-methylimidazolium hexafluorophosphate ([Bmim][PF6]), 1-hexyl-3-methylimidazolium hexafluorophosphate ([Hmim][PF6]), and 1-methyl-3-octylimidazolium hexafluorophosphate ([Omim][PF6]) from 283.15 to 343.15 K. Solubilities rise with a decrease in temperature and an increase in pressure. Highest solubility is in [Omim][PF6], followed by [Hmim][PF6], and [Bmim][PF6]. The new data were correlated by the NRTL model and by the Krichevsky-Ilinskays equation; both provide good agreement with the experimental data. Estimates are given for mixing enthalpy, entropy and Gibbs energy of dissolution.
Compounds
# Formula Name
1 C3H2F4 trans-1,3,3,3-tetrafluoropropene
2 C8H15F6N2P 1-butyl-3-methylimidazolium hexafluorophosphate
3 C10H19F6N2P 1-hexyl-3-methylimidazolium hexafluorophosphate
4 C12H23F6N2P 1-octyl-3-methylimidazolium hexafluorophosphate
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
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 42
  • POMD
  • 1
  • 3
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 42
  • POMD
  • 1
  • 4
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 42