Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Gas phase PVTx properties for binary mixtures of HFC-161 and HFC-134a

Chen, Q.[Qi], Tong, Y.[Yang], Hong, R.-h.[Rong-hua], Chen, G.-m.[Guang-ming]
Fluid Phase Equilib. 2011, 304, 1-2, 61-63
ABSTRACT
An experimental study of the pressure-volume-temperature-composition (PVTx) properties in the gas phase for binary mixtures of ethyl fluoride (HFC-161) and 1,1,1,2-tetrafluoroethane (HFC-134a) was conducted in the range of temperatures from 318.22 to 403.20 K, pressures from 1120.6 to 5767.0 kPa, densities from 0.494 to 3.974 mol dm-3, and compositions from 0.3203 to 0.9474 HFC-161 mole fractions. The measurements were performed with an isochoric cell apparatus. The uncertainties in the present work were estimated to be +-1.5 kPa for pressure and +-6mK for temperature. On the basis of the experimental PVTx property data, a truncated virial equation of state was developed for the HFC-161/134a binary system. This equation reproduces the experimental data in the gas phase within +-0.18% in pressure and within +-0.32% in density.
Compounds
# Formula Name
1 C2H2F4 1,1,1,2-tetrafluoroethane
2 C2H5F fluoroethane
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 - 2; Gas
  • Gas
  • ISOCHOR
  • 128