Thermodynamics Research Center / ThermoML | International Journal of Thermophysics

Thermodynamic Properties of Methanol in the Critical and Supercritical Regions

Abdulagatov, I. M.[Ilmutdin M.], Polikhronidi, N. G.[Nikolai G.], Abdurashidova, A. A., Kiselev, S. B., Ely, J. F.[James F.]
Int. J. Thermophys. 2005, 26, 5, 1327-1368
ABSTRACT
The isochoric heat capacity of pure methanol in the temperature range from 482 to 533 K, at near-critical densities between 274.87 and 331.59 kg *m.3, has been measured by using a high-temperature and high-pressure nearly constant volume adiabatic calorimeter. The measurements were performed in the singleand two-phase regions including along the coexistence curve. Uncertainties of the isochoric heat capacity measurements are estimated to be within 2%. The single- and two-phase isochoric heat capacities, temperatures, and densities at saturation were extracted from experimental data for each measured isochore. The critical temperature (Tc =512.78+-0.02 K) and the critical density (nc =277.49+- 2kg*m.3) for pure methanol were derived from the isochoric heat-capacity measurements by using the well-established method of quasi-static thermograms. The results of the CV VT measurements together with recent new experimental PVT data for pure methanol were used to develop a thermodynamically self-consistent Helmholtz free-energy parametric crossover model, CREOS97-04. The accuracy of the crossover model was confirmed by a comprehensive comparison with available experimental data for pure methanol and values calculated with various multiparameter equations of state and correlations. In the critical and supercritical regions at 0.98Tcless thanT less than1.5Tc and in the density range 0.35ncless thannless than1.65nc, CREOS97-04 represents all available experimental thermodynamic data for pure methanol to within their experimental uncertainties.
Compounds
# Formula Name
1 CH4O methanol
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 volume, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Small (less than 1 g) adiabatic calorimetry
  • 5
  • POMD
  • 1
  • Molar heat capacity at constant volume, J/K/mol ; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Small (less than 1 g) adiabatic calorimetry
  • 1
  • POMD
  • 1
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Quasistatic thermogram
  • 5
  • POMD
  • 1
  • Mass density, kg/m3 ; Gas
  • Temperature, K; Gas
  • Gas
  • Liquid
  • Quasistatit thermograms
  • 1
  • POMD
  • 1
  • Molar heat capacity at constant volume, J/K/mol ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Mass density, kg/m3; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • Small (less than 1 g) adiabatic calorimetry
  • 123