Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Gaseous absorption of fluorinated ethanes by ionic liquids

Liu, X.[Xiangyang], Qi, X.[Xuetao], Lv, N.[Nan], He, M.[Maogang]
Fluid Phase Equilib. 2015, 405, 1-6
ABSTRACT
Solubilities of 1,1-difluoroethane (R152a), pentafluoroethane (R125), fluoroethane (R161), 1,1,1-trifluoroethane (R143a) and 1,1,1,2-tetrafluoroethane (R134a) in trihexyltetradecylphosphonium bis(2,4,4-trimethylpentyl)phosphinate ([P(14)666][TMPP]) from 302.2 K to 343.6 K and up to 1.14 MPa are presented in this work. Effects of fluorine atoms of fluorinated ethanes, the cations and anions of ionic liquids on the solubility behaviors are investigated by comparing the solubilities of fluorinated ethanes and ethane in different ionic liquids. Moreover, the partial molar enthalpies and partial molar entropies of solutions at infinite dilution limit for R161, R143a, R125, R134a and R152a in [P(14)666][TMPP] are obtained. The experimental results are successfully correlated with a modified Krichevsky-Kasarnovsky equation.
Compounds
# Formula Name
1 C48H102O2P2 trihexyltetradecylphosphonium bis(2,4,4-trimethylpentyl)phosphinate
2 C2H2F4 1,1,1,2-tetrafluoroethane
3 C2H3F3 1,1,1-trifluoroethane
4 C2HF5 pentafluoroethane
5 C2H4F2 1,1-difluoroethane
6 C2H5F fluoroethane
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
  • 2
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Gas
  • Liquid
  • ISOPVT
  • 30
  • POMD
  • 2
  • 1
  • Mole fraction - 2 ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Gas
  • Liquid
  • Component 2 is not volatile
  • 30
  • POMD
  • 3
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 3; Liquid
  • Gas
  • Liquid
  • ISOPVT
  • 30
  • POMD
  • 3
  • 1
  • Mole fraction - 3 ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 3; Liquid
  • Gas
  • Liquid
  • Solvent component 2 is not volatile.
  • 30
  • POMD
  • 6
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 6; Liquid
  • Gas
  • Liquid
  • ISOPVT
  • 30
  • POMD
  • 6
  • 1
  • Mole fraction - 6 ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 6; Liquid
  • Gas
  • Liquid
  • Solvent component 2 is not volatile.
  • 30
  • POMD
  • 4
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 4; Liquid
  • Gas
  • Liquid
  • ISOPVT
  • 25
  • POMD
  • 4
  • 1
  • Mole fraction - 4 ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 4; Liquid
  • Gas
  • Liquid
  • Solvent component 2 is not volatile.
  • 25
  • POMD
  • 5
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 5; Liquid
  • Gas
  • Liquid
  • ISOPVT
  • 30
  • POMD
  • 5
  • 1
  • Mole fraction - 5 ; Gas
  • Temperature, K; Liquid
  • Mole fraction - 5; Liquid
  • Gas
  • Liquid
  • Solvent component 2 is not volatile.
  • 30