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efficiencies approaching 80 to 90%. Therefore, in order for these systems to be competitive isentropic efficiency needs to improve. 61.81% 0.01% Boiler % Expander % Regenerator % Condenser % Pump % 37.68% 0.01% 0.48% Figure 6.36: Exergy destruction of each component for water at optimized conditions In Figure 6.36 the opposite is true; the expander has the largest share of exergy destruction. This is due to the fact that water has a low power output during expansion and therefore is not using all the available exergy from state 1. Exergy destroyed in the pump is very low compared to R134a, due to the fact that the temperature and specific volume do not change as much during pumping with water. Regenerator exergy destroyed is also low with a value of 0.01% due to the very small temperature differences involved in the component. With R227ea (Figure 6.37), boiler and expander have similar exergy destruction shares. Due to the larger amount of regeneration needed for this fluid (due to 88PDF Image | Exergoeconomic Analysis and Optimization of ORC
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