Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Measurement of vapor liquid equilibria for the binary mixture of propylene (R-1270) + propane (R-290)

Ho, Q. N. N.[Quang Nhu], Yoo, K. S.[Kye Sang], Lee, B. G.[Byung Gwon], Lim, J. S.[Jong Sung]
Fluid Phase Equilib. 2006, 245, 1, 63-70
ABSTRACT
Isothermal vapor liquid equilibria data for the binary mixture of propylene (R-1270) + propane (R-290) at 273.15, 278.15, 283.15, 293.15, 303.15 and 313.15K were measured by using a circulation-type equilibrium apparatus. The experimental data were correlated with the Peng Robinson equation of state (PR-EOS) combined with the Wong Sandler mixing rule. It is confirmed that the data calculated by this equations of state are in good agreement with experimental data. The azeotropic behavior was not found in this mixture over range of temperature studied here.
Compounds
# Formula Name
1 C3H6 propene
2 C3H8 propane
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
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 6
  • POMD
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 6
  • POMD
  • 2
  • 1
  • Vapor or sublimation pressure, kPa ; Gas
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Gas
  • Liquid
  • EBULLIO:UFactor:4
  • 90
  • POMD
  • 2
  • 1
  • Mole fraction - 1 ; Gas
  • Mole fraction - 1; Liquid
  • Temperature, K; Liquid
  • Gas
  • Liquid
  • Chromatography
  • 90