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35000 30000 25000 20000 15000 10000 5000 0 Water (Original) R-123 (Original) Water R-245fa R-123 Benzene Ethanol R-236ea R-245ca 50 100 150 200 250 300 350 400 Exhaust Gas Temperature (°C) Figure 14. Work produced assuming minimum pressure limit is 170 kPa. Figure 13 and Figure 14 are very similar to Figure 5 and Figure 6. However, by allowing a lower minimum pressure (condensing pressure) the performances of non-refrigerants increase. From Figure 8, refrigerants do not require very low minimum pressure (condensing pressure), thus their performances were unaffected. In this case, the thermal efficiency of non-refrigerants increased by about 5% (for water at 250 °C) of the original thermal efficiency. The work also increased by about 9% (for water at 250 °C) of the original work. These percentages were calculated from the internal data. 5.3. Isentropic Efficiencies Another important assumption is the isentropic efficiency. I lowered the isentropic efficiencies of both the expander and the pump to 65% to see its influence. Figure 15 shows the new efficiency plot, and Figure 16 shows the new work plot. 22 Work per Unit Exhaust Mass Flow Rate (W/kg)PDF Image | Working Fluid Selections in Organic Rankine Cycle ICE
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