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peak system efficiency (Wei, Lu, Lu, & Gu, 2007). The research from Roy et al.(2011) revealed that non-regenerative ORC during superheating using R123 produces the maximum efficiencies and turbine work output for constant as well as variable heat source temperature conditions among four working fluids R12, R123, R-134a and R717 (Roy, 2011). Kuo, Chang, & Wang (2011) analyzed a 50 kW organic Rankine cycle system for the effect of heat exchangers. The results indicate that the dominant thermal resistance in the shell-and-tube condenser is on the shell side and the dominant thermal resistance is on the refrigerant side for the plate evaporator (Kuo, 2011). And Yamamoto, Furuhat, Arai, & Nori (2001) in their paper “ design and testing of a organic Rankine cycle” did the research for the optimal operation conditions of ORC theoretically and experimentally. They found that there are optimum operating conditions between the rotation speed and the turbine outlet and R-123 improves the cycle performance in the large extent comparing with traditional working fluid water (Yamamoto, 2001). 2.2.2 Working Fluids in ORC Power Cycle Considering the environmental impacts of ORC power plants, one of the disadvantages is the working fluid. Traditional organic working fluids used in ORC such as silicone oil, R245fa and R134a suffer from being excessively priced 26 | P a g ePDF Image | ZEOLITES DAY NIGHT DESORPTION CYCLE ADSORPTION CYCLE
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