Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Low pressure solubilities of CO2 in guanidinium trifluoromethanesulfonate-MDEA systems

Sairi, N. A.[Nor Asrina], Ghani, N. A.[Noraini Abd], Aroua, M. K.[Mohamed Kheireddine], Yusoff, R.[Rozita], Alias, Y.[Yatimah]
Fluid Phase Equilib. 2015, 385, 79-91
ABSTRACT
It is an urgent act to limit greenhouse gas emissions to avoid the harmful effects of climate changes. In this work, the binary and ternary systems of guanidinium trifluoromethanesulfonate ([gua][OTf]) in N-methyldiethanolamine (MDEA) and/or water were examined as alternative solvents for gas treatment process. The thermodynamic properties including density, r, viscosity, h, thermal expansion, ap and physical solubility of CO2 in the systems were measured as a function of molar composition with a temperature range of 293.2 333.2 K at 100 1000 kPa. The presence of [gua][OTf] accelerates CO2 absorption process. The present study offers equations of correlation providing a reliable prediction of the binary and ternary systems as a function of concentration. The linear equation, quadratic equation, extended Arhenius equation and Henry s Law equation have been applied to assess the validity of the finding. The CO2 solubilities in [gua][OTf] systems are found higher compared to other ILs in previous researches. Additionally, ANN modeling of the effective parameters was carried out and the composition of [gua][OTf] was proven as the key factor in maximizing the CO2 solubility.
Compounds
# Formula Name
1 C2H6F3N3O3S guanidinium trifluoromethanesulfonate
2 C5H13NO2 N-methyldiethanolamine
3 CO2 carbon dioxide
4 H2O water
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
  • 2
  • POMD
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Cone and plate viscometry
  • 3
  • POMD
  • 2
  • 4
  • 1
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 81
  • POMD
  • 2
  • 4
  • 1
  • Viscosity, Pa*s ; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Cone and plate viscometry
  • 48
  • POMD
  • 2
  • 4
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Cone and plate viscometry
  • 10
  • POMD
  • 2
  • 4
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 18
  • POMD
  • 4
  • 1
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Cone and plate viscometry
  • 28
  • POMD
  • 4
  • 1
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 18
  • POMD
  • 2
  • 3
  • 4
  • Mole fraction - 3 ; Liquid
  • Pressure, kPa - 3; Gas
  • Solvent: Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Titration method
  • 6
  • POMD
  • 3
  • 4
  • 1
  • Mole fraction - 3 ; Liquid
  • Pressure, kPa - 3; Gas
  • Solvent: Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Titration method
  • 6