Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

An experimental study of PVTx properties in the gas phase for binary mixtures of HFC-161 and HFC-32

Chen, Q.[Qi], Hong, R.-h.[Rong-hua], Chen, G.-m.[Guang-ming]
Fluid Phase Equilib. 2006, 243, 1-2, 156-160
ABSTRACT
An experimental study of the pressure volume temperature composition (PVTx) properties in the gas phase for binary mixtures of ethyl fluoride (HFC-161) + difluoromethane (HFC-32) was conducted in the range of temperatures from 303.179 to 403.190 K, pressures from 1182.9 to 5918.2 kPa, densities from 0.5754 to 3.2174 mol dm-3, and compositions from 0.1597 to 0.8989 mole fractions of HFC-161. The measurements were performed with an isochoric cell apparatus. The uncertainties in the present work were estimated to be +-1.5 kPa for pressure, +-6mK for temperature, and +-0.15% for composition. On the basis of the experimental PVTx property data, a truncated virial equation of state was developed for the binary HFC-161/32 system. This equation reproduced the experimental data in the gas phase within +-0.457% in pressure. The temperature dependence of the second virial coefficients, including the cross-virial coefficients for this system is also discussed.
Compounds
# Formula Name
1 C2H5F fluoroethane
2 CH2F2 difluoromethane
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
  • Amount density, mol/m3 ; Gas
  • Temperature, K; Gas
  • Pressure, kPa; Gas
  • Mole fraction - 1; Gas
  • Gas
  • ISOCHOR
  • 140