Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Thermodynamic studies on the phase equilibria of ternary {ionic liquid, 1-hexyl-3-methyl imidazolium chloride + D-fructose or sucrose + water} systems at 298.15 K and atmospheric pressure.

Zafarani-Moattar, M. T.[Mohammed Taghi], Shekaari, H.[Hemayat], Agha, E. M. H.[Elnaz Mazaher Haji]
Fluid Phase Equilib. 2017, 436, 38-46
ABSTRACT
In this work, to study vapor-liquid equilibria of ternary {ionic liquid, 1-hexyl-3-methyl imidazolium chloride + D-fructose or sucrose + water} systems, water activity measurements have been made using an improved isopiestic method at 298.15 K and atmospheric pressure. Segment-based local composition models of the Wilson, NRTL, modified NRTL, NRF-NRTL and UNIQUAC were accurately used to correlate the measured water activity data and parameters obtained from these models were utilized to calculate the unsymmetrical molal activity coefficients of the ionic liquid in the binary and saccharides in binary and ternary aqueous solutions. Furthermore, the Gibbs energy of transfer for D-fructose and sucrose from water to aqueous ionic liquid solutions has been determined from the activity coefficients of Dfructose and sucrose in binary and ternary solutions. Using McMillan-Mayer theory of solutions, pair and triplet interaction parameters and salting constant values were computed. Finally, from the magnitude of activity coefficients and the sign and magnitude of salting constant some information about solute-solute and solute-solvent interactions are obtained in these (saccharide + ionic liquid + water) systems.
Compounds
# Formula Name
1 C6H12O6 D-fructose
2 H2O water
3 C10H19ClN2 1-hexyl-3-methylimidazolium chloride
4 C12H22O11 D-sucrose
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
  • (Relative) activity - 2 ; Liquid
  • Molality, mol/kg - 3; Liquid
  • Molality, mol/kg - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 32
  • POMD
  • 4
  • 2
  • 3
  • (Relative) activity - 2 ; Liquid
  • Molality, mol/kg - 3; Liquid
  • Molality, mol/kg - 4; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 28
  • POMD
  • 1
  • 2
  • (Relative) activity - 2 ; Liquid
  • Molality, mol/kg - 1; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 15
  • POMD
  • 4
  • 2
  • (Relative) activity - 2 ; Liquid
  • Molality, mol/kg - 4; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 26
  • POMD
  • 2
  • 3
  • (Relative) activity - 2 ; Liquid
  • Molality, mol/kg - 3; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOPIE
  • 17