1,721,026 research outputs found
Solid-liquid equilibria for the dimethyl ether plus carbon dioxide binary system
No full textA recently built experimental setup was employed for the estimation of the solid-liquid equilibria of alternative refrigerants systems. The behavior of dimethyl ether (DME) + carbon dioxide was measured down to temperatures of 131.6 K. To confirm the reliability of the apparatus, the triple point of the DME was measured. The triple point data measured revealed a good consistency with the literature. The results obtained for the mixtures were corrected by the Rossini method and interpreted by means of the Schroder equation.</p
Solid-Liquid Equilibria for the Carbon Dioxide + 1,1-Tetrafluoroethane and Nitrous Oxide + 1,1-Tetrafluoroethane Systems
No full text
P-V-T-x and Vapor Liquid Equilibrium Properties of Pentafluoroethane (R125) + 1,1,1,3,3,3-Hexafluoroethane (R236fa) and 1,1,1,2-Tetrafluoroethane (R134a) + (R236fa) Systems Derived from Isochoric Measurements
No full textP-V-T-x and VLE Properties of Difluoromethane (R32) + 1,1,1,2,3,3-Hexafluoropropane (R236ea) and Pentafluoroethane (R125) + R236ea Systems Derived from Isochoric Measurements
No full textVirial coefficients from isochoric measurements for R236fa, R236ea, R32+R134a, R32+R236ea, R125+R236fa, and R134a+R236fa systems
No full textSydney, Australia, September 1999 - paper 41
Natural gas mixtures as working fluids for cascade cycles: a thermodynamic analysis
No full textGlasgow, Scotland, August 200
Isochoric PVTx measurements for the carbon dioxide + 1,1-difluoroethane binary system
Full text linkPVTx measurements for carbon dioxide (CO, R744) + 1,1-difluoroethane (CHCHF, R152a) for both the two-phase and the superheated vapor regions are presented. The measurements were taken with a constant volume apparatus at temperatures ranging from (223 to 343) K and pressures from (60 to 3890) kPa along eight isochores. The data obtained in the two-phase region were used to derive vapor-liquid equilibrium (VLB) parameters using a flash method with the Carnahan-Starling-De Santis equation of state (CSD EOS). The dew point was also found for each isochore from the intersection of the P-T sequences. Results from the superheated region were compared with those predicted from the CSD EOS. The complete set of data was also compared with the REFPROP 7.0 prediction
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