Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Vapor liquid equilibria of the 1,1-difluoroethane (HFC-152a) + isobutene system

Yun, Y.[Yongju], Im, J.[Jihoon], Shin, M. S.[Moon Sam], Lee, Y. -W.[Youn-Woo], Kim, H.[Hwayong]
Fluid Phase Equilib. 2008, 271, 1-2, 34-37
ABSTRACT
Isothermal vapor liquid equilibrium (VLE) data were measured for the 1,1-difluoroethane (HFC- 152a) + isobutene system in the temperature range from 273.15K to 348.15K at 15K intervals. The experiments were carried out with circulating-type apparatus with on-line gas chromatography. The VLE data were well correlated by the Peng Robinson Stryjek Vera equation of state with theWong Sandler mixing rules involving NRTL model, and the results show a positive azeotrope at each temperature. (C) 2008 Elsevier B.V. All rights reserved.
Compounds
# Formula Name
1 C2H4F2 1,1-difluoroethane
2 C4H8 2-methylpropene
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
  • 1
  • 2
  • Vapor or sublimation pressure, kPa ; Liquid
  • Mole fraction - 1; Gas
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • EBULLIO:UFactor:4
  • 83
  • POMD
  • 1
  • 2
  • Mole fraction - 1 ; Liquid
  • Mole fraction - 1; Gas
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • CHROM:UFactor:4
  • 83