Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols

Vale, V. R.[Vlad R.], Rathke, B.[Bernd], Will, S.[Stefan], Schroer, W.
J. Chem. Eng. Data 2011, 56, 4, 1330-1340
ABSTRACT
Liquid-liquid phase diagrams of binary mixtures of the ionic liquid 1-hexyl-3-methylimidazolium bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) with n-alkyl alcohols (hexan-1-ol, heptan-1-ol, octan-1-ol, nonan-1-ol, decan-1-ol, undecan-1-ol, dodecan-1-ol, and tetradecan-1-ol) are reported. By application of the cloud-point method on a set of samples, phase diagrams were obtained at atmospheric pressure over the temperature range (280 to 423) K. The investigated systems show partial miscibility with an upper critical solution temperature (UCST) between (306 and 401) K. With increasing chain length of the alcohol, the UCST shifts toward higher temperatures and slightly higher concentrations. Ising criticality was assumed in the numerical analysis of the phase diagrams. The analysis yielded the UCST, the corresponding critical composition, and the width and diameter parameters that characterize the shape of the phase diagrams. The temperature dependence of the diameter of the phase diagram, which determines the asymmetry of the phase diagram, is not linear as presumed by the rectilinear diameter rule of Cailletet-Mathias. Instead, as requested by the theory of complete scaling, it also depends on nonlinear, nonanalytical contributions that are the leading terms when the critical solution point is approached. The shapes of the phase diagrams of the investigated solutions are very similar when the data are represented in terms of corresponding-states variables.
Compounds
# Formula Name
1 C12H19F6N3O4S2 1-hexyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide
2 C6H14O hexan-1-ol
3 C7H16O heptan-1-ol
4 C8H18O octan-1-ol
5 C9H20O nonan-1-ol
6 C10H22O decan-1-ol
7 C11H24O 1-undecanol
8 C12H26O dodecan-1-ol
9 C14H30O 1-tetradecanol
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
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mass fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:2
  • 13
  • POMD
  • 3
  • 1
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mass fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:4
  • 14
  • POMD
  • 4
  • 1
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mass fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:2
  • 13
  • POMD
  • 5
  • 1
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mass fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:4
  • 12
  • POMD
  • 6
  • 1
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mass fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:4
  • 14
  • POMD
  • 7
  • 1
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mass fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:2
  • 10
  • POMD
  • 8
  • 1
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mass fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:2
  • 13
  • POMD
  • 9
  • 1
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mass fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:4
  • 10