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Figure 10: Heating curve for the cycle with reheat and recup T-Hot T-Cold 0 1e6 2e6 3e6 4e6 5e6 6e6 7e6 8e6 9e6 1e7 1.1e7 1.2e7 1.3e7 1.4e7 1.5e7 1.6e7 Cumulative Duty Btu/hr Figure 12. Heating curve for the cycle with reheat and recuperation Figure 11: Cooling curve for the cycle with reheat and recup T-Hot T-Cold 0 1e6 2e6 3e6 4e6 5e6 6e6 7e6 8e6 9e6 1e7 1.1e7 1.2e7 Cumulative Duty Btu/hr Figure 13. Cooling curve for the cycle with reheat and recuperation 3.2.5 ORC with Recuperation and Reheat using Mixed Hydrocarbons The advantages of ORC with mixed hydrocarbons working fluid was explained earlier. To identify the impact of the mixed working fluids on the cycle shown in Figure 11, we used mixed working fluids consisting of pentane/heptane, pentane/iso-hexane, pentane/iso-butane, and iso- butane/iso-hexane. Six combinations of the above working fluids were analyzed (Table 7). For the sake of comparison with the pure component working fluid, the results for a mixture of pentane/iso-butane (95% pentane, 5% iso-butane) are presented here. This working fluid gave the highest efficiency (20.7%) among the cycles analyzed. All the assumptions and working conditions assumed for the pure component case were applied here. 18 TEMPERATURE F 320 360 400 440 480 90 100 110 120 130 140 150 160 170 180 520 560 600 TEMPERATURE FPDF Image | Modular Trough Power Plant Cycle and Systems Analysis
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