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heat after expansion heats up the swimming pool which acts as the cold sink (condenser) for the unit (Eneftech Innovation SA, 2011). Figure 2.2: Eneftech scroll expander geometry modified from (Eneftech Innovation SA, 2011) Thermoeconomic optimization and evaluation is performed on organic Rankine cycle systems in literature. An analysis carried out by Quoilin et al (2011) compares different working fluids such as R245fa, n-butane and n-pentane. Thermodynamic efficiency, economics and profitability are the objective functions evaluated. N-butane produces an economical optimum of 2136€/kW (2787$/kW in 2012) at an efficiency of 4.47%. Maximum thermodynamic efficiency for n-butane in the system is 5.22%. One of the things the study takes into account is the component sizing and the associated cost when changing temperatures and other parameters in the system. One parameter, evaporating temperature, is used to show the effect of change on the component costs as it increases. Overall component costs for the system go down; the biggest change is the cost of the 11PDF Image | Exergoeconomic Analysis and Optimization of ORC
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