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

Gaseous Absorption of trans-1-Chloro-3,3,3-trifluoropropene in Three Immidazolium-Based Ionic Liquids

He, Maogang, Pan, Pei, Yang, Feng, Wang, Tao, Liu, Xiangyang
J. Chem. Eng. Data 2018, 63, 5, 1780-1788
ABSTRACT
In this work, the solubilities and trans-1-chloro-3,3,3-trifluoropropene (R1233zd(E)) diffusion coefficients of refrigerant in three imidazolium ionic liquids were measured at temperatures from 303.1 to 343.2 K, pressures up to 0.14 MPa. The ionic liquids include 1-hexyl-3-methyl-imidazolium 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)amide trifluoromethanesulfonate ([HMIM][Tf2N]), ([HMIM][TfO]) and 1-hexyl-3-methyl-imidazolium tetrafluoroborate([HMIM][BF4]). The Non-Random Two-Liquid (NRTL) activity coefficient model was employed to correlate the experimental solubility data successfully, the AAD between the measured data and calculated values for the solubilities of R1233zd(E) in [HMIM][Tf2N], [HMIM][TfO] and [HMIM][BF4] are 3.1 %, 2.5 % and 4.0 %, respectively. The Wilke-Chang equation was used to correlate diffusion coefficients, the relative deviations between experimental results and the values calculated are most within 10 %. Meanwhile, the solubility and diffusivity of refrigerant gases R32, R125, R152a, R161, R143a, R1234yf, R1234ze(E) and R1233zd(E) in ionic liquids [HMIM][Tf2N], [HMIM][TfO] and [HMIM][BF4] were compared and analyzed.
Compounds
# Formula Name
1 C3H2ClF3 (E)-1-chloro-3,3,3-trifluoroprop-1-ene
2 C12H19F6N3O4S2 1-hexyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide
3 C11H19F3N2O3S 1-hexyl-3-methylimidazolium trifluoromethanesulfonate
4 C10H19BF4N2 1-hexyl-3-methylimidazolium tetrafluoroborate
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
  • 30
  • POMD
  • 1
  • 2
  • Binary diffusion coefficient, m2/s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • phase equilibration
  • 5
  • POMD
  • 1
  • 3
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 30
  • POMD
  • 1
  • 3
  • Binary diffusion coefficient, m2/s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • phase equilibration
  • 5
  • POMD
  • 1
  • 4
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 30
  • POMD
  • 1
  • 4
  • Binary diffusion coefficient, m2/s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Gas
  • phase equilibration
  • 5