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Figure 6-10 shows the effect of changes in the waste heat source mass flow rate on the net power output of the proposed dual heat source ORC plant. The graph shows that an increase in the exhaust to stack mass flow rate for any given foul gas mass flow rate causes an increase in the net power output of the plant. The reason is because increase in waste heat source mass causes an increase in the working fluid mass flow rate (see Figure 6-11) through the cycle, and this gives rise to an increase in the amount of power 8 7 6 5 4 3 2 1 0 Foul Gas Mass Flow rate (kg/s) 1 3 5 9 10 11 12 13 14 15 Exhaust to Stack Mass Flow Rate (kg/s) Figure 6–11: Effect of Variation in Waste Heat Mass Flow Rate on Working Fluid Requirement produced by the working fluid. Figure 6-12 shows the effect of variation in waste heat mass flow rate on the cooling water requirement in the condenser. The graph shows that an increase in waste heat source mass causes a corresponding increase in cooling water requirement. This is 140 R245fa Working Fluid Mass Flow Rate (kg/s)PDF Image | OPTIMISING THERMAL ENERGY RECOVERY
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