Phase equilibria of HFC mixtures: Binary mixtures of trifluoromethane plus 1,1-difluoroethane and trifluoromethane plus 1,1,1-trifluoroethane at 283.15 and 293.15 K

Authors
Lim, JSPark, KHLee, BG
Issue Date
2002-05
Publisher
AMER CHEMICAL SOC
Citation
JOURNAL OF CHEMICAL AND ENGINEERING DATA, v.47, no.3, pp.582 - 586
Abstract
Isothermal vapor-liquid equilibria for the binary mixtures of trifluoromethane (R-23) + 1,1-difluoroethane (HFC-152a) and trifluoromethane + 1,1,1-trifluoroethane (HFC-143a) were measured at 283.15 and 293.15 K. The experiments were carried out with a circulation-type equilibrium apparatus with the measurement of temperature, pressure, and the compositions of the liquid and vapor phases. The experimental data were correlated with the Peng-Robinson equation of state using the Wong and Sandler mixing rules and the Carnahan - Starling - Desantis (CSD) equation of state. Calculated results with these equations showed good agreement with the experimental data, but the Peng-Robinson equation of state gave more accurate predictions for the binary systems. Azeotropic behavior has not been found in either of these mixtures.
Keywords
ALTERNATIVE REFRIGERANT MIXTURES; VAPOR-LIQUID-EQUILIBRIA; PENTAFLUOROETHANE HFC-125; MIXING RULE; STATE; DIFLUOROMETHANE; ISOBUTANE; EQUATION; SYSTEMS; ALTERNATIVE REFRIGERANT MIXTURES; VAPOR-LIQUID-EQUILIBRIA; PENTAFLUOROETHANE HFC-125; MIXING RULE; STATE; DIFLUOROMETHANE; ISOBUTANE; EQUATION; SYSTEMS; phase equilibria; HFC; HFC-23; HFC-152a; HFC-143a; P-R EOS; CSD EOS
ISSN
0021-9568
URI
https://pubs.kist.re.kr/handle/201004/139584
DOI
10.1021/je0102311
Appears in Collections:
KIST Article > 2002
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