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Figure 6.6: System exergy efficiency for water ...................................................................................... 63 Figure 6.7: Expander isentropic efficiency for water........................................................................... 64 Figure 6.8: Electrical power output for R227ea..................................................................................... 65 Figure 6.9: System exergy efficiency for R227ea................................................................................... 65 Figure 6.10: Expander isentropic efficiency for R227ea .................................................................... 66 Figure 6.11: Electrical power output for R245fa ................................................................................... 67 Figure 6.12: System exergy efficiency for R245fa ................................................................................. 67 Figure 6.13: Expander isentropic efficiency for R245fa ..................................................................... 68 Figure 6.14: Electrical power output for iso-butane............................................................................ 69 Figure 6.15: System exergy efficiency for iso-butane .......................................................................... 69 Figure 6.16: Expander isentropci efficiency for iso-butane .............................................................. 70 Figure 6.17: Electrical power output for iso-pentane ......................................................................... 70 Figure 6.18: System exergy efficiency for iso-pentane........................................................................ 71 Figure 6.19: Expander isentropic efficiency for iso-pentane............................................................ 71 Figure 6.20: Electrical power output for dimethyl ether ................................................................... 72 Figure 6.21: System exergy efficiency for dimethyl ether.................................................................. 73 Figure 6.22: Expander isentropic efficiency for dimethyl ether...................................................... 73 Figure 6.23: Optimized values of pressure ratio and degree of superheat for all working fluids........................................................................................................................................................................ 75 Figure 6.24: System exergy efficiency for various working fluids .................................................. 77 Figure 6.25: System energy efficiency for various working fluids.................................................. 78 Figure 6.26: Expander isentropic efficiency for various working fluids ...................................... 79 Figure 6.27: Electricity cost rate for various working fluids ............................................................ 80 Figure 6.28: Electrical output for various working fluids .................................................................. 81 Figure 6.29: T-s diagram for dimethyl ether at optimal operating conditions .......................... 82 Figure 6.30: T-s diagram for toluene at optimal operating conditions......................................... 82 Figure 6.31: RPM for various working fluids at optimized conditions ......................................... 83 Figure 6.32: Pressure difference between Input and output of expander at optimized conditions.............................................................................................................................................................. 84 Figure 6.33: Output torque for various working fluids at optimized conditions...................... 85 Figure 6.34: Heat input for various working fluids at optimized conditions ............................. 86 Figure 6.35: Exergy destruction of each component for R134a at optimized conditions ..... 87 Figure 6.36: Exergy destruction of each component for water at optimized conditions....... 88 Figure 6.37: Exergy destruction of each component for R227ea at optimized conditions ... 89 Figure 6.38: Exergy destruction of each component for R245fa at optimized conditions.... 89 Figure 6.39: Exergy destruction of each component for toluene at optimized conditions ... 90 Figure 6.40: Exergy destruction of each component for iso-butane at optimized conditions ................................................................................................................................................................................... 90 Figure 6.41: Exergy destruction of each component for acetone at optimized conditions... 91 viiPDF Image | Exergoeconomic Analysis and Optimization of ORC
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