Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Desulfurization of fuel-oils with [C2mim][NTf2]: A comparative study

Rodriguez-Cabo, B.[Borja], Soto, A., Arce, A.
J. Chem. Thermodyn. 2013, 57, 248-255
ABSTRACT
A tendency to use polysubstituted pyridinium-based ionic liquids for desulfurization of fuel-oils is being very remarkable during last years. Are these ones the most suitable ionic liquids for this purpose? The possibility of using a much cheaper ionic liquid, 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide, has been studied in this work. With this aim, LLE data of the {[C2mim][NTf2] + thiophene + toluene}, {[C2mim][NTf2] + thiophene + n-hexane} and {[C2mim][NTf2] + pyridine + n-hexane} ternary systems have been obtained at T = 298.15 K and atmospheric pressure. The NRTL and UNIQUAC models have been used to correlate the obtained data. Solute distribution ratios and selectivities have been calculated and a comparison with data obtained previously for other ionic liquids has been established. It was found that both cation and anion clearly affect to these thermodynamic parameters. According not just to solubility, but also in terms of selectivity and cost, [C2mim][NTf2] can be a competitive desulfurization solvent.
Compounds
# Formula Name
1 C4H4S thiophene
2 C6H14 hexane
3 C8H11F6N3O4S2 1-ethyl-3-methylimidazolium bis((trifluoromethyl)sulfonyl)imide
4 C5H5N pyridine
5 C7H8 toluene
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
  • 3
  • Mole fraction - 2 ; Liquid mixture 1
  • Mole fraction - 1 ; Liquid mixture 2
  • Mole fraction - 3 ; Liquid mixture 2
  • Mole fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 2
  • Temperature, K; Liquid mixture 2
  • Liquid mixture 1
  • Liquid mixture 2
  • Chromatography
  • Chromatography
  • Chromatography
  • 12
  • POMD
  • 2
  • 4
  • 3
  • Mole fraction - 4 ; Liquid mixture 2
  • Mole fraction - 2 ; Liquid mixture 1
  • Mole fraction - 4 ; Liquid mixture 1
  • Mole fraction - 3; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 1
  • Temperature, K; Liquid mixture 1
  • Liquid mixture 2
  • Liquid mixture 1
  • Chromatography
  • Chromatography
  • Chromatography
  • 10
  • POMD
  • 5
  • 1
  • 3
  • Mole fraction - 5 ; Liquid mixture 1
  • Mole fraction - 5 ; Liquid mixture 2
  • Mole fraction - 1 ; Liquid mixture 2
  • Mole fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 2
  • Temperature, K; Liquid mixture 2
  • Liquid mixture 1
  • Liquid mixture 2
  • Chromatography
  • Chromatography
  • Chromatography
  • 12
  • POMD
  • 2
  • 3
  • Mole fraction - 3 ; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Temperature, K; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • Chromatography
  • 1
  • POMD
  • 1
  • 3
  • Mole fraction - 1 ; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Temperature, K; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • Chromatography
  • 1
  • POMD
  • 5
  • 3
  • Mole fraction - 5 ; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Temperature, K; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • Chromatography
  • 1