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
Link To Document :
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