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Operating Heat point Exchanger Pre-heater Evaporator Table5: Specificationheatexchangerofpointsfrom1ito4i Waste Geometric Pressure Source specification (Pa) drop Volume (m3 ) 0.049 0.346 0.864 0.4239 0.005 0.027 0.148 0.100 0.200 - 0.335 0.93 0.0320 0.1300 0.01714 0.0003 0.1172 0.0304 0.0320 0.1300 0.0171 0.0030 1i 2i 3i 4i Superheater Pre-heater Evaporator Superheater Pre-heater Evaporator Superheater Pre-heater Evaporator Superheater Cooling water Aftercooler Exhaust gases EGR EGR Cooling Water Aftercooler Exhaust gases EGR - Intercooler Exhaust gases Aftercooler Exhaust gases EGR EGR Intercooler Exhaust gases Aftercooler Exhaust gases EGR EGR L=0.4m ; D=0.7 m L=6 m ; D=0.48 m L=9.6 m ; D=0.6 m L=0.6 m ; D=0.3 m Lx=0.1 m;Ly=0.05 m; Lz=0.05 m L=0.3m ; D=0.6 m L=2.8 m ; D=0.46 m L=2.64 m ; D=0.39 m L=2.64 m ; D=0.2 m No Superheating L=3.6m ; D=0.61 m L=5.4m ; D=0.83 m L=1.8 m ; D=0.27 m L=3.6 m ; D=0.381 m L=1.2 m ; D=0.27 m Lx=0.07 m; Ly=0.05 m ; Lz=0.07 m L=1.26 m ; D=0.61 m L=2.3m ; D=0.23 m L=1.8 m ; D=0.27 m L=3 m ; D=0.34 m L=2.3 m ; D=0.25 m Lx=0.1 m; Ly=0.05 m ; Lz=0.01 m 35 125 210 50 279 2634 949 11000 3518 - 835 1001 107 699 313 107 1600 125 107 699 313 307 26PDF Image | Methodology to design a bottoming Rankine cycle
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