Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Pressure-volume-temperature-composition relations for carbon dioxide + pyrrolidinium-based ionic liquid binary systems

Makino, T.[Takashi], Kanakubo, M.[Mitsuhiro], Umecky, T.[Tatsuya], Suzuki, A.[Akira], Nishida, T.[Tetsuo], Takano, J.[Jun]
Fluid Phase Equilib. 2013, 360, 253-259
ABSTRACT
The pressure-volume-temperature-composition relations for CO2 + pyrrolidinium-based ionic liquid systems were measured over the pressure range up to 6 MPa at T=(298.15, 313.15, 333.15) K. Three ionic liquids were studied in the present work: N-methyl-N-propylpyrrolidinium bis(trifluoromethanesulfonyl)amide ([Pyr13][TFSA]), N-methoxymethyl-N-methylpyrrolidinium bis(trifluoromethanelsulfonyl)amide ([Pyr1,1O1][TFSA]), and N-methoxymethyl-N-methylpyrrolidinium bis(fluorosulfonyl)amide ([Pyr1,1O1][FSA]). The pressure dependence of CO2 solubility indicates that CO2 molecules are dissolved physically in the three ionic liquids. The mole fraction scaled solubility of CO2 in [Pyr1,1O1][TFSA] is almost the same as that in [Pyr13][TFSA], and [Pyr1,1O1][FSA] showed the smallest solubility at certain pressures and temperatures. On the other hand, the molarity scaled solubility of CO2 in [Pyr1,1O1][TFSA] was nearly equal to that in [Pyr1,1O1][FSA]. The CO2 solubility of [Pyr13][TFSA] was smaller than the other two ionic liquids. The molar volume and density of ionic liquid phase decrease monotonically with an increase of mole fraction of CO2. The volume expansion of liquid phase was not almost dependent of temperature but composition of CO2 under the conditions investigated.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 C10H18F6N2O4S2 1-methyl-1-propylpyrrolidinium bis[(trifluoromethyl)sulfonyl]imide
3 C9H16F6N2O5S2 1-(methoxymethyl)-1-methylpyrrolidinium 1,1,1-trifluoro-N-[(trifluoromethyl)sulfonyl]methanesulfonamide
4 C7H16F2N2O5S2 1-(methoxymethyl)-1-methylpyrrolidinium bis(fluorosulfonyl)amide
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
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 12
  • POMD
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Unspecified
  • 12
  • POMD
  • 2
  • Electrical conductivity, S/m ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Unspecified
  • 11
  • POMD
  • 1
  • 2
  • Mole fraction - 1 ; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Volumetric analysis
  • 27
  • POMD
  • 1
  • 2
  • Molar volume, m3/mol ; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Other PVT measurement
  • 27
  • POMD
  • 1
  • 3
  • Mole fraction - 1 ; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Volumetric analysis
  • 27
  • POMD
  • 1
  • 3
  • Molar volume, m3/mol ; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Other PVT measurement
  • 27
  • POMD
  • 1
  • 4
  • Mole fraction - 1 ; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Volumetric Analysis
  • 27
  • POMD
  • 1
  • 4
  • Molar volume, m3/mol ; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Other PVT measurement
  • 27