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SUPERCRITICAL CO2 CYCLES FOR GAS TURBINE COMBINED CYCLE

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SUPERCRITICAL CO2 CYCLES FOR GAS TURBINE COMBINED CYCLE ( supercritical-co2-cycles-for-gas-turbine-combined-cycle )

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Primary HX Recuperator CX-1 Generator Pump Turbine Water return Water supply Figure 1: Simple recuperated sCO2 cycle More complex cycle architectures, such as the โ€œrecompression cycleโ€ [7] enable very high thermodynamic efficiency (defined as net power output / heat input, or ๐‘Š /๐‘„ ) for heat sources that are internally recirculated, such as nuclear and CSP. For these applications, maximum power output is achieved when the thermodynamic efficiency of the cycle is maximized. Because these cycles perform poorly for non-recirculated sources, such as bottoming applications, they are not considered here. On the other hand, heat recovery cycles are designed to maximize power output by simultaneously achieving high thermodynamic efficiency and minimizing the unrecovered enthalpy to the greatest allowable extent. As a result, for the same heat source temperature, the direct conversion efficiency of heat recovery cycles is lower than that of the typically considered cycles (recompression, partial cooling, etc.). However, heat recovery cycles will deliver a significantly higher output power from a sensible enthalpy heat source because of their increased utilization of available enthalpy. POWER CYCLE SYSTEM DESCRIPTION Supercritical CO2 power cycles have several distinguishing characteristics that influence their design and application. The foremost characteristic is that the pressure between the pump discharge and the turbine inlet is well above the critical pressure (7.38 MPa), ๐‘œ๐‘œ๐‘œ ๐‘–๐‘– 4

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