Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Excess molar enthalpies of the ternary mixture n-propanol + acetic acid + water at 313.15 K and atmospheric pressure

Letyanina, I.[Irina], Tsvetov, N.[Nikita], Toikka, A.[Alexander]
Fluid Phase Equilib. 2015, 405, 150-156
ABSTRACT
Excess molar enthalpies, HE m, for the ternary mixture n-propanol (n-PrOH) + acetic acid (AcOH) + water (H2O) were measured at 313.15 K and atmospheric pressure using the Setaram C80 calorimeter. The data for initial binary sub-systems were taken from the literature and correlated with the Redlich-Kister equation. The experimental results on the ternary system were fitted by means of different variable degree polynomials. Smooth representations of the results were used to construct constant excess molar enthalpy contours on Roozeboom diagram. The capability of the NRTL model to predict excess molar enthalpies for the ternary systems based on the data for the binary sub-systems was considered.
Compounds
# Formula Name
1 C3H8O propan-1-ol
2 C2H4O2 acetic acid
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
  • 2
  • 1
  • 3
  • Excess molar enthalpy (molar enthalpy of mixing), kJ/mol ; Liquid
  • Mole fraction - 1; Liquid
  • Mole fraction - 2; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Flow calorimetry
  • 59