Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Experimental study of the isochoric heat capacity of tert-butanol in the critical and supercritical regions

Radzhabova, L. M., Stepanov, G. V.[Genadii V.], Abdulagatov, I. M.[Ilmutdin M.]
Fluid Phase Equilib. 2011, 309, 2, 128-144
ABSTRACT
The one- and two-phase isochoric heat capacities of tert-butanol in the critical and supercritical regions have been measured with a high-temperature and high-pressure nearly constant-volume adiabatic calorimeter. The measurements were made in the temperature range from 296 K to 524 K for 21 liquid and 7 vapor isochores from 70.56 kg m-3 to 763.98 kg m-3. The isochoric heat capacity jump (quasistatic thermograms supplemented by the sensor of adiabatic control) technique was used to accurately measure of the phase transition parameters in the critical region. The total experimental uncertainty of density, temperature, and isochoric heat capacity measurements were estimated to be 0.02%, 15 mK, and 2.3%, respectively. The critical temperature (T_c = 506.35 +/- 0.2 K) and the critical density (rho_c = 268.1 =/- 2 kg m-3) for tert-butanol were extracted from the measured saturated properties near the critical point. The measured heat capacity and saturated density data near the critical point have been analyzed and interpreted in terms of extended scaling equations for the selected thermodynamic paths (critical isochore and coexistence curve) to accurately calculate the values of the asymptotical critical amplitude. The experimentally derived value of the critical amplitude ratio A+0/A-0 = 0.525 is in good agreement with the value predicted by various scaling theories. The measured thermodynamic properties of tert-butanol near the critical point were also interpreted in terms of the complete scaling theory of critical phenomena. In particular, the contributions of the complete and incomplete scaling terms on the coexistence-curve singular diameter were estimated. The Yang-Yang anomaly of strength parameter R_mu = -0.036 for tert-butanol was estimated using derived second temperature derivatives of pressure and chemical potential. The measured values of saturated one-phase and two-phase liquid and vapor isochoric heat capacities and saturated thermal properties together with reported vapor.pressure data were used to calculate a number of other derived thermodynamic properties of tert-butanol at saturation near the critical point.
Compounds
# Formula Name
1 C4H10O 2-methylpropan-2-ol
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
  • Critical temperature, K ; Liquid
  • Liquid
  • Gas
  • Derived from heat capacity data
  • 1
  • POMD
  • 1
  • Critical density, kg/m3 ; Liquid
  • Liquid
  • Gas
  • Derived from heat capacity data
  • 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)
  • Cu2O-jacketed adiabatic calorimeter
  • 11
  • POMD
  • 1
  • Molar heat capacity at constant volume, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Mass density, kg/m3; Liquid
  • Liquid
  • Cu2O-jacketed adiabatic calorimeter
  • 15
  • POMD
  • 1
  • Molar heat capacity at constant volume, J/K/mol ; Fluid (supercritical or subcritical phases)
  • Mass density, kg/m3; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • Cu2O-jacketed adiabatic calorimeter
  • 322
  • POMD
  • 1
  • Molar heat capacity at constant volume, J/K/mol ; Liquid
  • Mass density, kg/m3; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Cu2O-jacketed adiabatic calorimeter
  • 137