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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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6.2 Optimization of the System 50 45 40 35 30 25 20 15 10 5 0 Pressure Ratio Degree of Superheat ( ̊C) Fluid Name Figure 6.23: Optimized values of pressure ratio and degree of superheat for all working fluids To optimize the system two independent variables are chosen to optimize the objective function. In this case the function to be optimized is exergy efficiency, and the two independent variables are the pressure ratio (PR) and the amount of superheat (Tsh). While the function of exergy efficiency may not be dependent on pressure ratio and super heat directly, these two variables influence the work output and the amount of heat input needed. These two characteristics are what influence the exergy efficiency equation since it is dependant both on electrical work output and amount of heat input. Figure 6.23 shows the values of PR and Tsh that are optimized for each working fluid tested. All the dry fluids such as R227ea, R134a and n-pentane need high degrees of super 75 Values

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