Abstract:
Isothermal vapor−liquid equilibrium data are presented for the
1,1,2,2-tetrafluoroethylene and 1,1,2,3,3,3-hexafluoroprop-1-ene binary system
at (248.14, 263.01, and 282.89) K, with pressures ranging from (0.12 to 2.35)
MPa. An apparatus based on the “static−analytic” method, equipped with a
movable rapid online sampler−injector (ROLSI), was used to undertake the
measurements. The combined expanded uncertainties are estimated at 0.11 K,
4 kPa, and 0.012 and 0.009 for the temperature, pressure, and the equilibrium
liquid and vapor mole fractions, respectively. The experimental data were
correlated with the Peng−Robinson equation of state using the Mathias
−Copeman α function, together with the Wong−Sandler mixing rule utilizing
the nonrandom two-liquid activity coefficient model.
