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Hence, by fixing the sizes of the components using the above mentioned criteria, the performance of the plant during variations in waste heat temperature, mass flow rate and cooling water temperature is obtained as follows. 6.6.1 Effect of Variation in Foul Gas and Exhaust to Stack Temperature at Fixed Cooling Water Temperature and Condenser Pressure Although the plant was designed with foul gas and exhaust to stack temperature of 120oC and 164oC respectively, however, in a real system, there is every tendency that the waste heat temperatures mentioned above will deviate from the base load condition. In this case study, the waste heat temperature from the foul gas was assumed to vary from 110 to 130oC while that of the exhaust to stack was assumed to vary from 156 to 168oC. Figure 6–7 shows the graph depicting the effect of variation in the waste heat temperature on the net power output of the dual heat source ORC system. The graph shows that for any given waste heat temperature from the exhaust to stack, the net power output from the plant increases as the foul gas temperature increases. This occurs because as the foul gas temperature increases for any given exhaust to stack temperature; more working fluid is vaporized in the evaporator (i.e. more working fluid is used in the system) (see Figure 6–8) and this gives rise to more power output. 136PDF Image | OPTIMISING THERMAL ENERGY RECOVERY
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