Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion

Domanska, U.[Urszula], Marciniak, A.[Andrzej]
J. Chem. Thermodyn. 2005, 37, 6, 577-585
ABSTRACT
The (liquid + liquid) equilibrium (LLE) of 20 binary systems containing 1-hexyloxymethyl-3-methyl-imidazolium tetra- fluoroborate ([C6H13OCH2mim][BF4]) with aliphatic hydrocarbons (n-pentane, or n-hexane, or n-heptane, or n-octane), aromatic hydrocarbons (benzene, or toluene, or ethylbenzene, or o-xylene, or m-xylene, or p-xylene), cyclohexane and 1-hexyloxymethyl-3- methyl-imidazolium bis(trifluoromethylsulfonyl)-imide ([C6H13OCH2mim][Tf2N]) in aliphatic hydrocarbons (n-hexane, or n-heptane), aromatic hydrocarbons (benzene, or toluene, or ethylbenzene, or o-xylene, or m-xylene, or p-xylene) and cyclohexane was carried out by using a dynamic method from T = 290 K to the boiling temperature of the solvent. In this work, a systematic study of the impact of different factors on the phase behaviour of alkoxy-imidazolium-based ionic liquids with hydrocarbons has been presented. All systems examined showed upper critical solution temperature (UCST) behaviour, with low solubility of the ionic liquid in n-alkanes and cycloalkanes and high solubility in aromatic hydrocarbons. An increase in the alkyl chain length of n-alkane, or at benzene ring resulted in an increase in the UCST. The choice of anion was shown to have large impact on the UCST of the system: by changing the anion [BF4]? to [Tf2N], the solubility dramatically increased and the UCST decreased. The relative hydrocarbon affinity for different anions observed was [BF4]? less than [Tf2N]. The thermophysical characteristic of ionic liquids was detected by differential scanning calorimetry (DSC). The experimental results of LLE have been correlated using the binary parameters of NRTL equation. The average rootmean- square deviation of the equilibrium mole fraction for all the calculated values was 0.0044.
Compounds
# Formula Name
1 C6H14 hexane
2 C13H21F6N3O5S2 1-(hexyloxymethyl)-3-methylimidazolium bis((trifluoromethyl)sulfonyl)amide
3 C7H16 heptane
4 C6H6 benzene
5 C7H8 toluene
6 C8H10 ethylbenzene
7 C8H10 1,2-dimethylbenzene
8 C8H10 1,3-dimethylbenzene
9 C8H10 1,4-dimethylbenzene
10 C5H12 pentane
11 C11H21BF4N2O 1-hexyloxymethyl-3-methylimidazolium tetrafluoroborate
12 C8H18 octane
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
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 2; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:16
  • 8
  • POMD
  • 3
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 2; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:16
  • 9
  • POMD
  • 4
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 2; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 19
  • POMD
  • 4
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 2
  • Mole fraction - 2; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • VISOBS:UFactor:8
  • 19
  • POMD
  • 5
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 2
  • Mole fraction - 2; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • VISOBS:UFactor:8
  • 18
  • POMD
  • 5
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 2; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 18
  • POMD
  • 6
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 2; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:16
  • 18
  • POMD
  • 6
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 2
  • Mole fraction - 2; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • VISOBS:UFactor:8
  • 18
  • POMD
  • 7
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 2
  • Mole fraction - 2; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • VISOBS:UFactor:8
  • 18
  • POMD
  • 7
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 2; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:16
  • 18
  • POMD
  • 8
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 2
  • Mole fraction - 2; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • VISOBS:UFactor:8
  • 20
  • POMD
  • 8
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 2; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:16
  • 20
  • POMD
  • 9
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 2; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 17
  • POMD
  • 9
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 2
  • Mole fraction - 2; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • VISOBS:UFactor:8
  • 17
  • POMD
  • 10
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 5
  • POMD
  • 1
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 6
  • POMD
  • 3
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 7
  • POMD
  • 12
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:16
  • 7
  • POMD
  • 4
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 2
  • Mole fraction - 11; Liquid mixture 2
  • Pressure, kPa; Liquid mixture 2
  • Liquid mixture 2
  • Liquid mixture 1
  • VISOBS:UFactor:16
  • 9
  • POMD
  • 4
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 9
  • POMD
  • 5
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 7
  • POMD
  • 6
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 7
  • POMD
  • 7
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:16
  • 11
  • POMD
  • 8
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:16
  • 8
  • POMD
  • 9
  • 11
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 11; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:16
  • 8