Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols

Xing, N.[Nannan], Yang, L.[Lili], Wei, J.[Jie], Gu, C.[Chuang], Li, Z.[Zhe], Guan, W.[Wei]
J. Chem. Thermodyn. 2017, 115, 171-179
ABSTRACT
The density and viscosity of multicomponent solutions play an important role in industrial areas concerning mass and heat transfer, as well as fluid flow. To expand the potential application of ILs, it is important to know the physicochemical properties of ILs with solvents for ILs widely used. The density and viscosity for binary mixtures of ionic liquid (IL) [C2py][DCA] with ethanol, 1-propanol and 2-propanol were measured across the entire range of mole fraction (x1 = 0.0000 1.0000) at T = (288.15 318.15) K. The excess molar volumes, VE, were calculated and well fitted by Redlich Kister equation. The obtained VE are negative values over the whole composition range and it means that there is greater interaction between the ions and the alcohol molecules. The values of Dg have been applied to description of the viscosity deviation of the mixtures from the ideal one, but the equation of excess Gibbs energy of activation for viscous flow, DG E, for mixture cannot be derived from Dg. And more serious is that an incorrect equation of DG E is widely used in the literature. In view of this situation, we put forward a new concept the relative viscosity of mixture, gr. On a basis of the new concept, a correct equation of DG E is obtained. The values of gr and DG E of mixtures [C2py][DCA]+alcohol over the whole composition range were calculated. The values of gr are less than one and DG E are negative so that this result means that the interaction among ions becomes weaker due to ion solvation. The DG E values of the mixtures [C2py] [DCA]+alcohol were well fitted by the Redlich Kister equation. Using the Redlich Kister s parameters, the values of viscosity for mixtures [C2py][DCA]+alcohols were estimated and the estimated g(est.) is in good agreement with the experimental g. In order to test the reliability of the method proposed in this work, we also deal with the data of mixtures for [HDBU]IM + H2O, [BDBU]IM + H2O and [Mim]Ac + Alcohols in the literatures. The results also prove that this method is reasonable.
Compounds
# Formula Name
1 C2H6O ethanol
2 C9H10N4 1-ethylpyridinium dicyanamide
3 C3H8O propan-1-ol
4 C3H8O propan-2-ol
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
  • 7
  • POMD
  • 1
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 7
  • POMD
  • 3
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 7
  • POMD
  • 3
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 7
  • POMD
  • 4
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 7
  • POMD
  • 4
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 7
  • POMD
  • 1
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 77
  • POMD
  • 1
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 77
  • POMD
  • 3
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 77
  • POMD
  • 3
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 77
  • POMD
  • 4
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 77
  • POMD
  • 4
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 2; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Falling or rolling sphere viscometry
  • 77