Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Volumetric, ultrasonic and viscometric studies of solute solute and solute solvent interactions of l-threonine in aqueous-sucrose solutions at different temperatures

Nain, A. K.[Anil Kumar], Pal, R.[Renu], Neetu
J. Chem. Thermodyn. 2013, 64, 172-181
ABSTRACT
Densities, q of solutions of l-threonine in aqueous-sucrose solvents 5%, 10%, 15%, and 20% of sucrose, w/w in water at T = (293.15, 298.15, 303.15, 308.15, 313.15, and 318.15) K; and ultrasonic speeds, u and viscosities, g of these solutions at 298.15, 303.15, 308.15, 313.15, and 318.15 K were measured at atmospheric pressure. From these experimental results, the apparent molar volume, V/, limiting apparent molar volume, V / and the slope, Sv, apparent molar compressibility, Ks;/, limiting apparent molar compressibility, K s;/ and the slope, Sk, transfer volume, V /;tr , transfer compressibility, K s;/;tr , limiting apparent molar expansivity, E /, Hepler s constant, d2V /=dT2P, Falkenhagen coefficient, A, Jones Dole coefficient, B and hydration number, nH have been calculated. The results have been interpreted in terms of solute solvent and solute solute interactions in these systems. The Gibbs energies of activation of viscous flow per mole of solvent, Dl 1 and per mole of solute, Dl2 were also calculated and discussed in terms of transition state theory. It has been observed that there exist strong solute solvent interactions in these systems and these interactions increase with increase in sucrose concentration in solution.
Compounds
# Formula Name
1 C4H9NO3 L-threonine
2 C12H22O11 D-sucrose
3 H2O water
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
  • 3
  • Speed of sound, m/s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Linear variable-path acoustic interferometer
  • 5
  • POMD
  • 2
  • 1
  • 3
  • Mass density, kg/m3 ; Liquid
  • Solvent: Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Molality, mol/kg - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 216
  • POMD
  • 2
  • 1
  • 3
  • Speed of sound, m/s ; Liquid
  • Solvent: Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Molality, mol/kg - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • LVPAI:WF =
  • 225
  • POMD
  • 2
  • 1
  • 3
  • Viscosity, Pa*s ; Liquid
  • Solvent: Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Molality, mol/kg - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 180
  • POMD
  • 2
  • 3
  • Mass density, kg/m3 ; Liquid
  • Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Pycnometric method
  • 24
  • POMD
  • 2
  • 3
  • Speed of sound, m/s ; Liquid
  • Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • LVPAI:WF =
  • 20
  • POMD
  • 2
  • 3
  • Viscosity, Pa*s ; Liquid
  • Mass fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 20
  • POMD
  • 1
  • 3
  • Speed of sound, m/s ; Liquid
  • Temperature, K; Liquid
  • Molality, mol/kg - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • LVPAI:WF =
  • 40