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c .-C 25- C 1I 1 c0 , E20- c 18 itself does not appear to be a dominant factor in the cost of the total system, but the performance of this subsystem has a profound influence on the total system cost. In summary, each application requires careful study from a total systems viewpoint to de- termine the most cost effective system. d d* r0l 'y 15- A 8 .- Basis of Calculations (all cycles) Working Fluid - Toluene Lower Cycle Temp - 150°F Generator Efficiency - . 9 0 Regenerator Efficiency - .90 Feed Pump Efficiency - . 6 0 c 'CI w01 c 10- Ux 0I Figure 17. hIIII 300 400 500 6 0 0 Peak Cycle Temperature in OF Calculated Cycle Efficiency vs. Peak Cycle Temperature for Cycles Which Are Identical with the Exception of Turbine Efficiency TABLE 111 Comparison of System Parameters for the Rankine Cycle Systems Represented in Figure 17. Peak Cycle Temperature is 550°F in Each Case P a r a m e t e r Input Heat Rate (Btu/Hr/100 kWe) Regenerator Heat Rate (Btu/Hr/ 100 kWe) Condenser Heat Rate (Btu/Hr/100 kW,) Mass Flaw Rate (Ib/Hr/lOO kWe) Pump Work (hp/ 100 kW,) Cycle A ET = . 6 1,849,000 695,000 1,468,000 8.430 8.08 Cycle B ET = . 7 5 1,535.000 470,900 1,154,000 6,670 6.39 Cycle C . ET = . 9 1.329.000 324,200 948.200 5,520 5.29 I. .*PDF Image | RANKINE CYCLE ENERGY CONVERSION SYSTEM DESIGN CONSIDERATIONS FOR LOW AND INTERMEDIATE TEMPERATURE SENSIBLE HEAT SOURCES
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