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Solar Trough Organic Rankine Electricity System (STORES) Stage 1: Power Plant Optimization and Economics

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Solar Trough Organic Rankine Electricity System (STORES) Stage 1: Power Plant Optimization and Economics ( solar-trough-organic-rankine-electricity-system-stores-stage )

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800 700 600 500 400 300 200 100 0 0 25 50 75 100 125 150 175 200 Duty, MMBtu/hr Heating Fluid Toluene Cycle Butane Cycle Cooling Fluid Figure 4.3.4: Toluene/Butane Cascade Cycle For all of the above cases, the use of recuperation results in even higher cycle thermal efficiencies. The Maloney-Robertson aqua ammonia cycle was also investigated. It takes a mixture of ammonia and water, partially vaporizes it and separates the ammonia-enriched vapor in a separator. The vapor passes through the turbine while the water-rich liquid is cooled in the recuperator and then mixed with the turbine exhaust stream before it goes into the condenser. This allows the condenser pressure to be lower than if only the ammonia rich vapor is condensed. This simple Maloney-Robertson cycle can operate as a topping cycle but must operate at too high a pressure when the temperature is in the 600 oF range. Therefore, the Maloney-Robertson cycle is considered as a bottoming cycle to an ORC topping cycle. 20

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