Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

PvT and thermal-pressure coefficient measurements of diethyl ether (DEE) in the critical and supercritical regions

Polikhronidi, N. G., Batyrova, R. G., Abdulagatov, I. M., Stepanov, G. V., Wu, J. T.
J. Chem. Thermodyn. 2012, 53, 67-81
ABSTRACT
The pressures (P) and its temperature derivatives or thermal-pressure coefficient of DEE have been measured in the near- and supercritical regions as a function of temperature along the various liquid and vapour isochores. Measurements were made in the immediate vicinity of the liquid-gas phase transition and the critical points (single- and two-phase regions) using a high-temperature, high-pressure, nearly constant-volume adiabatic piezo-calorimeter. The constant-volume adiabatic calorimeter previously used for C_v measurements was additionally supplied with high accurate strain gauge (calibrated piezoelectric transducer) to measure simultaneously the PvT, C_v vT, and thermal-pressure coefficient. Measurements were made along 17 liquid and vapour isochores in the range from (212.6 to 534.6) kg m-3 and at temperatures from (347 to 575) K and at pressures up to 18 MPa. The quasi-static thermo- (reading of PRT, T-tau plot) and barograms (readings of the high accurate strain gauge, P-tau plot) techniques were used to accurate measure of the phase transition parameters at saturation curve. Temperatures at the liquid-gas phase transition curve for each measured density (isochore) and the critical parameters (T_c and rho_c) for DEE were obtained using the quasi-static thermograms technique. The expanded uncertainty of the pressure and its temperature derivative measurements at the 95% confidence level with a coverage factor of k = 2 is estimated to be 0.05% and (0.12 to 1.5)% (depending on temperature and pressure), respectively. The measured pressures and temperature derivatives have been used to calculate the internal pressure (or energy volume coefficient). The effect of pressure and temperature on the internal pressure near the critical point was studied. The measured values of thermal-pressure coefficient were used to determine accurately the behaviour of second temperature derivative near the critical point and compared with our previous isochoric heat capacity measured results. The measured and derived thermodynamic properties of DEE near the critical point were interpreted in terms of theory of critical phenomena.
Compounds
# Formula Name
1 C4H10O diethyl ether
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
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • ISOCHOR
  • 17
  • POMD
  • 1
  • Mass density, kg/m3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • ISOCHOR
  • 130
  • POMD
  • 1
  • Mass density, kg/m3 ; Gas
  • Temperature, K; Gas
  • Pressure, kPa; Gas
  • Gas
  • ISOCHOR
  • 15