• Title of article

    Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353 K and pressures up to 4.16 MPa

  • Author/Authors

    Madani، نويسنده , , Hakim and Valtz، نويسنده , , Alain and Coquelet، نويسنده , , Christophe and Meniai، نويسنده , , Abdeslam Hassen and Richon، نويسنده , , Dominique، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2008
  • Pages
    6
  • From page
    68
  • To page
    73
  • Abstract
    Isothermal vapor–liquid equilibrium data are reported for the binary system of hexafluoroethane and 1,1,1,2-tetrafluoroethane in the temperature range 263–353 K and in the pressure range 0.2–4.2 MPa. A reliable “static-analytic” method taking advantage of two online micro-capillary ROLSI™ samplers is used for all the measurements. The data are correlated using our in-house (ThermoSoft) thermodynamic software based on the Peng–Robinson equation of state, the Mathias–Copeman alpha function, the Wong–Sandler mixing rules, and the NRTL model.
  • Keywords
    VLE data , refrigerants , R116 , MODELING , Supercritical gas solubility , critical point , Phase diagram determination , R134a
  • Journal title
    Fluid Phase Equilibria
  • Serial Year
    2008
  • Journal title
    Fluid Phase Equilibria
  • Record number

    1986992