Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Density, viscosity and excess properties in the trihexyltetradecylphosphonium chloride ionic liquid/methanol cosolvent system

McAtee, Z. P.[Zachery P.], Heitz, M. P.[Mark P.]
J. Chem. Thermodyn. 2016, 93, 34-44
ABSTRACT
The volumetric and viscosity behaviors of binary mixtures of (trihexyl(tetradecyl)phosphonium chloride ionic liquid + methanol) ([P14,6,6,6 + ][Cl ] + MeOH) have been described across the entire range of mol fraction [P14,6,6,6 + ][Cl ] (xIL = 0 to 1) and over a temperature range of (290.15 to 313.15) K at p = 0.1 MPa. All binary mixtures were liquids completely miscible. The experimental data was used to calculate the excess molar properties of these solutions. The variation of density was used to compute excess molar volumes, and partial molar volumes of each component and the excess thermal expansion coefficients . For each of these excess parameters, the deviations were observed to be negative over the entire range of mole fraction and temperature. Viscosity deviations from the ideal mixtures were calculated from the measured viscosities. Additionally, temperature dependent viscosities were observed to follow an Arrhenius activation model and the activation energy, Ea, of viscous flow was computed. Combined viscosity and volumetric data were used to calculate the excess Gibbs free energy of activation of viscous flow. The results from the excess solution properties behaviors have been discussed in terms of molecular interactions and support the presence of strong interactions in solution. These interactions are typical of IL aggregation. In this IL/cosolvent system the most significant changes occur up to xIL 0.4.
Compounds
# Formula Name
1 C32H68ClP trihexyl(tetradecyl)phosphonium chloride
2 CH4O methanol
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
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 9
  • POMD
  • 1
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 8
  • POMD
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 9
  • POMD
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 9
  • POMD
  • 2
  • 1
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 91
  • POMD
  • 2
  • 1
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 65