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operating pressure of the evaporator. The liquid thermal conductivity was based on the saturated liquid thermal conductivity at the evaporator pressure. The latent heat was based on latent heat of each working fluid at the evaporator pressure. Based on these criteria, and knowing that some of the information for r-245fa was not available, each of the working fluids were suggested that further calculations be done so a decision could be made based on the solar field requirements. Table 2 shows the results of these working fluid selection criteria. Table 2 - Working fluid selection criteria. 62 butane isobutane pentane isopentane neopentane r-134a r-245fa no 4 0.96 4 1.41 4 0.33 4 0.41 4 0.72 3 3.79 data 0.81 213 190 224 222 266 523 no data 0.0852 296.3 0.0895 248.0 0.1103 322.3 0.1068 301.5 0.0920 250.9 0.0803 52.4 0.0875 151.5 Working Fluid toxicity boiling point Pressure (MPa) flash point (K) liquid thermal conductivity (W/m·K) latent heat (kJ/kg)PDF Image | WORKING FLUID SELECTION FOR AN INCREASED EFFICIENCY HYBRIDIZED GEOTHERMAL-SOLAR THERMAL POWER PLANT IN NEWCASTLE, UTAH
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