## 3 Results
\begin{table}
\begin{tabular}{c c c c c c c c c c c c} \hline \hline Component & \(\dot{C}_{D,K}\) & \(\dot{C}_{D,K}^{EN}\) & \(\dot{C}_{D,K}^{CX}\) & \(\dot{C}_{D,K}^{XY}\) & \(\dot{C}_{D,K}^{UV}\) & \(\dot{C}_{D,K}^{IN}\) & \(\dot{C}_{D,K}^{ENAV}\) & \(\dot{C}_{D,K}^{EXAV}\) & \(\dot{C}_{D,K}^{EXUN}\) & \(\dot{C}_{D,K}^{EXUN}\) & \(\dot{C}_{D,K}^{EXUN}\) & F (\%) \\  & (USD.S-1) & (USD.S-1) & (USD.S-1) & (USD.S-1) & (USD.S-1) & (USD.S-1) & (USD.S-1) & (USD.S-1) & (USD.S-1) & (USD.S-1) & \\ \hline Coupling Pump & 1.18E-06 & 6.73E-07 & 5.03E-07 & 1.45E-07 & 1.03E-06 & 8.31E-08 & 5.89E-07 & 4.28E+01 & 4.41E-07 & 87.48 \\ HTF Pump & 9.51E-06 & 8.57E-06 & 9.40E-07 & 1.19E-06 & 8.33E-06 & 1.07E-06 & 7.50E-06 & 9.88E+00 & 8.23E-07 & 81.5 \\ ORC Condenser & - & - & - & - & - & - & - & - & - & - & - \\ ORC Evaporator & 0.0011 & 1.02E-03 & 8.40E-05 & 1.06E-04 & 9.94E-04 & 9.82E-05 & 9.18E-04 & 7.64E+00 & 7.59E-05 & 92.25 \\ ORC Pump & 9.86E-04 & 7.42E-04 & 2.43E-04 & 1.83E-04 & 8.03E-04 & 1.38E-04 & 6.05E-04 & 2.47E+01 & 1.95E-04 & 74.92 \\ ORC Recuperator & 3.39E-04 & 2.92E-04 & 1.01E-04 & 1.04E-04 & 2.89E-04 & 7.70E-05 & 2.13E-04 & 2.56E+01 & 7.42E-05 & 70.7 \\ ORC Turbine & 0.0033 & 2.95E-03 & 3.54E-04 & 7.06E-04 & 2.59E-03 & 6.30E-04 & 2.32E-03 & 1.07E+01 & 2.79E-04 & 84.41 \\ Solar & & & & & & & & & & \\ Field(Collector) & 0 & 0.00E+00 & 0.00E+00 & 0.00E+00 & 0.00E+00 & 0.00E+00 & 0.00E+00 & 3.58E+01 & 0.00E+00 & 44.14 \\ Steam Economizer & 0.0014 & 1.10E-03 & 3.03E-04 & 5.38E-04 & 8.62E-04 & 4.22E-04 & 6.75E-04 & 2.16E+01 & 1.86E-04 & 68.01 \\ Steam Evaporator & 0.0045 & 3.26E-03 & 1.24E-03 & 1.41E-03 & 3.09E-03 & 1.02E-03 & 2.24E-03 & 2.76E+01 & 8.55E-04 & 72.03 \\ Steam Pump & 4.72E-05 & 4.31E-05 & 4.14E-06 & 5.88E-06 & 4.14E-05 & 5.37E-06 & 3.77E-05 & 8.77E+00 & 3.63E-06 & 90.26 \\ Steam Super heater & 9.64E-04 & 7.06E-04 & 2.58E-04 & 2.84E-04 & 6.80E-04 & 2.08E-04 & 4.98E-04 & 2.67E+01 & 1.82E-04 & 75.03 \\ Steam Turbine & 2.20E-03 & 1.99E-03 & 2.12E-04 & 3.80E-04 & 1.82E-03 & 3.43E-04 & 1.65E-03 & 9.64E+00 & 1.75E-04 & 91.14 \\ Topping & - & - & - & - & - & - & - & - & - & - & - \\ Condenser & - & - & - & - & - & - & - & - & - & - & - \\ \hline \hline \end{tabular}
\end{table} 
Table 16: Advanced exergy-economic analysis for hybrid solar-geothermal cycle (SGPP). The economic improvement potential of elements was determined by the evaluation of their avoidable/endogenous exergy destruction cost rates. In Table 16, the highest value of \(\dot{C}^{EN,AV}_{D,K}\) was of the steam evaporator (1.02E-03 USD.S\({}^{-1}\)), followed by the ORC turbine (6.30E-04 USD.S\({}^{-1}\)) and the steam economizer (4.22E-04 USD.S\({}^{-1}\)). This fact implies that by improving these components, the system exergy destruction cost rate can be reduced significantly and the components must be considered themselves, instead of other components. It should be noticed that the values of \(\dot{C}^{EX}_{D,K}\) in the steam evaporator (3.03E-04 USD.S\({}^{-1}\)) and the ORC turbine (3.54E-04 USD.S\({}^{-1}\)) were higher, demonstrating that if the performance of the remaining components rises, the exergy destruction cost rate of these components will decrease. The steam evaporator had the highest value of \(\dot{C}^{EN,AV}_{D,K}\) (1.02E-03 USD.S\({}^{-1}\)) and we can reduce the sizable portion of its exergy destruction cost by improving exergy efficiency of the other component. Additionally, \(\dot{C}^{EX,AV}_{D,K}\) in the Coupling Pump was huge (4.28E+01 USD.S\({}^{-1}\)) in comparison with the other components, associated with the exergy destruction cost rate of other components. With regard to the auxiliary heater, the results showed that the amount of \(\dot{C}^{EN}_{D,K}\) in the solar field was around zero because the exergy destruction cost rate of auxiliary heater is dependent on other components and only half of \(\dot{C}^{EX}_{D,K}\) can be avoided by using new technologies in other components. Table 17 indicates the results of the advanced exergo-environmental analysis for the GPP cycle.