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CHAPTER 2: Organic Rankine Cycle – Literature Review Evaporator Working fluid HTF Cooling medium 1 Expander 2 2a Brine Pump 4a 4 Pump 3 Generator Cooling tower Recuperator Condenser Geothermal zone Figure 2-10 Schematic of a geothermal ORC binary power cycle Madhawa Hettiarachchi et al. (2007) proposed a cost-effective design criterion as the ratio of total heat exchanger area to net power output for the ORC driven by geothermal heat. They optimized the proposed objective function (OF) for four organic fluids using steepest descent method. It was shown that the choice of working fluid can greatly affect the OF and for some fluids the difference was more than twice. The minimum OF was achieved by the ammonia while R123 and n-pentane showed higher cycle thermal efficiency. Liu et al. (2013) carried out thermodynamic investigation of the ORC with a wet cooling system using five hydrocarbons driven by geothermal heat in the temperature range of 100°C to 150°C and reinjection temperature of 70°C. The results indicated that the optimal condensation temperature for maximum power output is around 29.6°C when the cooling water inlet temperature is about 20°C. Isobutane showed the highest power output at inlet temperatures 29 | P a g e Injection well Production wellPDF Image | SMALL-SCALE RADIAL INFLOW TURBINE FOR WHR ORC
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