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

Densities and Viscosities of Sugar Alcohol Aqueous Solutions

Zhu, C.[Chunying], Ma, Y.[Youguang], Zhou, C.[Chuanling]
J. Chem. Eng. Data 2010, 55, 9, 3882-3885
ABSTRACT
In this paper, the densities and the viscosities for butane-1,2,3,4-tetrol (erythritol), (2S,3R,4R,5R)-hexane-1,2,3,4,5,6-hexol (sorbitol), (2R,3R,4R,5R)-hexane-1,2,3,4,5,6-hexol (mannitol), (2R,3R,4S)-pentane-1,2,3,4,5-pentol (xylitol), and 2-(hydroxymethyl)-6-[4,5,6-trihydroxy-2-(hydroxymethyl)oxan-3-yl]oxyoxane-3,4,5-triol (maltitol) aqueous solutions of various mole concentrations have been determined at T = (293.15, 303.15, 313.15, and 323.15) K. The experimental data for the viscosities of sugar alcohol aqueous solutions present a nonlinear relation to the temperature or concentration. The exponential model was used to correlate the experimental data for viscosities, with the maximum average deviation of 3.7 %. The experimental data for the densities of sugar alcohol aqueous solutions show a linear relation to the temperature or concentration considerably well. The linear equation was used to correlate the data for densities, and the maximum average deviation between the experimental data and the calculated values is 0.056 %.
Compounds
# Formula Name
1 C4H10O4 meso-1,2,3,4-butanetetrol
2 H2O water
3 C6H14O6 mannitol
4 C6H14O6 D-sorbitol
5 C5H12O5 xylitol
6 C12H24O11 4-O-.alpha.-D-glucopyranosyl-D-glucitol
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
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • CAPTUB:UFactor:4
  • 40
  • POMD
  • 1
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:32
  • 40
  • POMD
  • 3
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 3; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • CAPTUB:UFactor:4
  • 32
  • POMD
  • 3
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 3; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:32
  • 32
  • POMD
  • 4
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 4; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • CAPTUB:UFactor:4
  • 40
  • POMD
  • 4
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 4; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:32
  • 40
  • POMD
  • 5
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 5; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • CAPTUB:UFactor:4
  • 40
  • POMD
  • 5
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 5; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:32
  • 40
  • POMD
  • 6
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 6; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • CAPTUB:UFactor:4
  • 40
  • POMD
  • 6
  • 2
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Amount concentration (molarity), mol/dm3 - 6; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • VIBTUB:UFactor:32
  • 40