Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Heat capacity and phase behaviour of aqueous solutions of triethylene glycol monopentyl ether. Two point scaling analysis

Wasiak, M.[Michal], Tkaczyk, M.[Mariola], Piekarski, H.[Henryk]
Fluid Phase Equilib. 2017, 431, 16-23
ABSTRACT
The specific heat capacities of triethylene glycol monopentyl ether aqueous solutions have been measured from 278.15 K to 338.15 K, over the wide concentration range by DSC. The apparent and partial molar heat capacities were calculated and the two-point scaling theory was used to analyze these data. Obtained results were discussed in terms of aggregation taking place in the solution and influence of the temperature on this process. The separation line between single-phase solution and two-phase system was determined using scanning calorimetry.
Compounds
# Formula Name
1 C11H24O4 ethanol, 2-[2-[2-(pentyloxy)ethoxy]ethoxy]-
2 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
  • 1
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • DSC
  • 9
  • POMD
  • 2
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • DSC
  • 9
  • POMD
  • 2
  • 1
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Molality, mol/kg - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • DSC
  • 22
  • POMD
  • 2
  • 1
  • Molar heat capacity at constant pressure, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Molality, mol/kg - 1; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • DSC
  • 343