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Exergoeconomic Analysis and Optimization of ORC

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Exergoeconomic Analysis and Optimization of ORC ( exergoeconomic-analysis-and-optimization-orc )

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0.2950 0.2900 0.2850 0.2800 0.2750 0.2700 0.2650 Working Fluid Figure 6.26: Expander isentropic efficiency for various working fluids Figure 6.26 shows the isentropic efficiency of the expander at the optimized conditions. For most fluids this is the maximum or near maximum value at the given conditions. Isentropic efficiency is considered to be at a maximum if the pressure after the isochoric pressure building section is the same as the condenser pressure. If the pressure is higher or lower, throttling or additional work are needed. These additional processes are considered irreversibility’s since they do not contribute to useful work output and waste potential work output. High pressure ratios introduce additional leakage since leakage mass flow rate is a function of input and output pressures. Dimethyl ether has the highest value of isentropic efficiency of 29.22% while n-pentane has the lowest with 27.45%. These values are very low and show that this expander has significant losses due to friction and leakage. 79 Isentropic Efficiency

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