G. Dinicola et al., VAPOR-LIQUID-EQUILIBRIUM (VLE) PROPERTIES OF R-32-134A SYSTEM DERIVEDFROM ISOCHORIC MEASUREMENTS(R), Fluid phase equilibria, 153(1), 1998, pp. 143-165
Two methods developed for deriving Vapor-Liquid-Equilibrium (VLE) data
from isochoric measurements are presented in this paper. The first, s
o-called 'flash' method depends on a knowledge of the volumetric prope
rties, estimated by means of an appropriate model; in the present case
, the Carnahan-Starling-De Santis (CSD) equation of state (EOS) was us
ed to predict the mixture's behavior. As for the second, so-called 'mo
del-free' method, the first step is based on dew point evaluation by i
nterpolating experimental P-T sequences. The dew point value obtained
is then used to derive VLE data, again using the Camahan-Starling-De S
antis equation of state. Two hundred twenty-five experimental P-V-T-x
experimental data were obtained using a constant volume apparatus and
12 different binary mixture compositions prepared with the halogenated
refrigerants difluoromethane (R-32) and 1,1,1,2-terafluoromethane (R-
134a}, in a temperature range of 240-360 K. From these experimental da
ta the VLE properties were derived by using the two methods. A compari
son of the results obtained against data in the literature shows consi
stent agreement within the experimental uncertainty. (C) 1998 Elsevier
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