International audienceIsothermal vapor–liquid equilibrium data (P–x–y) are presented for ethene + 2,2,3-trifluoro-3-(trifluoromethyl)oxirane mixtures at six temperatures in the range 258.38–307.38 K, and pressures up to 4.54 MPa. Experimental P–x–y data were measured using an apparatus based on the " static-analytic " method. The experimental data were correlated with a model composed of the Peng–Robinson equation of state using the Mathias–Copeman alpha function, Wong–Sandler mixing rules and the NRTL local composition model. The thermodynamic model accurately represents the experimental VLE data over the entire temperature range investigated
International audienceIsothermal vapour–liquid equilibrium data for the difluoromethane (R32)-1,1,1,...
International audienceIsothermal vapor-liquid equilibrium (VLE) data are presented for the system he...
International audienceIsothermal vapour-liquid equilibrium data for the difluoromethane (R32)-1,1,1,...
International audienceIsothermal vapor-liquid equilibrium data are reported for ethylene + 1,1,2,3,3...
International audience_______________________________________________________________________ In thi...
International audienceNovel isothermal (P-x-y) vapour-liquid equilibrium data are reported at three ...
International audienceIsothermal (vapour + liquid) equilibrium data (P–x–y) are presented for ...
Isothermal vapor–liquid equilibrium data are presented for the 1,1,2,3,3,3-hexafluoroprop-1-ene and ...
International audienceIsothermal vapor-liquid equilibrium (VLE) data for the binary systems R-744 + ...
International audienceIsothermal vapor-liquid equilibrium data are reported for the binary system of...
International audiencePerformances of systems using refrigerants are highly dependent on the selecti...
International audienceThe isothermal vapor–liquid equilibrium (VLE) data for two hexafluoroethane (R...
International audienceThe isothermal vapor–liquid equilibrium (VLE) data for two hexafluoroethane (R...
A recirculation apparatus in which the vapor phase was forced through the liquid was used to measure...
International audienceIsothermal vapour–liquid equilibrium data for the difluoromethane (R32)-1,1,1,...
International audienceIsothermal vapour–liquid equilibrium data for the difluoromethane (R32)-1,1,1,...
International audienceIsothermal vapor-liquid equilibrium (VLE) data are presented for the system he...
International audienceIsothermal vapour-liquid equilibrium data for the difluoromethane (R32)-1,1,1,...
International audienceIsothermal vapor-liquid equilibrium data are reported for ethylene + 1,1,2,3,3...
International audience_______________________________________________________________________ In thi...
International audienceNovel isothermal (P-x-y) vapour-liquid equilibrium data are reported at three ...
International audienceIsothermal (vapour + liquid) equilibrium data (P–x–y) are presented for ...
Isothermal vapor–liquid equilibrium data are presented for the 1,1,2,3,3,3-hexafluoroprop-1-ene and ...
International audienceIsothermal vapor-liquid equilibrium (VLE) data for the binary systems R-744 + ...
International audienceIsothermal vapor-liquid equilibrium data are reported for the binary system of...
International audiencePerformances of systems using refrigerants are highly dependent on the selecti...
International audienceThe isothermal vapor–liquid equilibrium (VLE) data for two hexafluoroethane (R...
International audienceThe isothermal vapor–liquid equilibrium (VLE) data for two hexafluoroethane (R...
A recirculation apparatus in which the vapor phase was forced through the liquid was used to measure...
International audienceIsothermal vapour–liquid equilibrium data for the difluoromethane (R32)-1,1,1,...
International audienceIsothermal vapour–liquid equilibrium data for the difluoromethane (R32)-1,1,1,...
International audienceIsothermal vapor-liquid equilibrium (VLE) data are presented for the system he...
International audienceIsothermal vapour-liquid equilibrium data for the difluoromethane (R32)-1,1,1,...