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The supercritical carbon dioxide power cycle: Comparison to other advanced power cycles

机译:超临界二氧化碳功率循环:与其他高级功率循环的比较

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This paper consists of three parts. The first part presents a mostly thermodynamic comparison of the supercritical carbon dioxide (S-CO2) cycle to helium Brayton, superheated steam, and supercritical steam cycles. Issues that contribute to plant cost are discussed. The second part presents an economic comparison of a gas-cooled reactor coupled to S-CO2 direct, helium Brayton direct.. and superheated steam indirect cycles. The results indicate savings of up to 30% if the steam indirect cycle is replaced with the direct S-CO2 cycle. Compared to the helium direct cycle, the savings can reach 15%. The third part describes the optimization and potential of the indirect S-CO2 cycle and the effect of reheating. The indirect cycles of helium to S-CO2 and lead bismuth to S-CO2 are studied to assess the performance of gas-to-gas and liquid metal or liquid salt indirect cycles, respectively. It is shown that although the indirect cycle of helium to S-CO2 is feasible, it poses challenges in the intermediate heat exchanger design and suffers efficiency losses due to the large power consumption of the main circulators. Gas indirect cycles are well suited for liquid metal or liquid salt reactors. Further, the study indicates that employing reheat is economically unattractive for the indirect cycle of helium to S-CO2 because of efficiency reduction from pressure losses in reheaters and interconnecting ducting and additional capital cost. A similar conclusion was also reached for the indirect cycles of liquid metal or liquid salt to S-CO2 even though pumping power is very small. This is because of the additional cost of an intermediate liquid metal (or liquid salt) loop, which needs to be added since it is not possible to place all heat exchangers for reheat inside the reactor vessel.
机译:本文由三部分组成。第一部分主要介绍了超临界二氧化碳(S-CO2)循环与氦布雷顿,过热蒸汽和超临界蒸汽循环的热力学比较。讨论了影响工厂成本的问题。第二部分介绍了与S-CO2直接,氦布雷顿直接和间接蒸汽过热循环耦合的气冷反应器的经济比较。结果表明,如果将蒸汽间接循环替换为直接S-CO2循环,则最多可节省30%。与氦气直接循环相比,可节省15%。第三部分描述了间接S-CO2循环的优化和潜力以及再加热的影响。研究了氦气到S-CO2的间接循环和铋铋到S-CO2的间接循环,分别评估了气对气和液态金属或液态盐的间接循环的性能。结果表明,尽管将氦气间接转化为S-CO2是可行的,但它给中间热交换器的设计带来了挑战,并且由于主循环器的大功率消耗而导致效率损失。气体间接循环非常适合液态金属或液态盐反应器。此外,研究表明,由于再热器中压力损失和互连管道的效率降低以及额外的资本成本,对于氦气间接转化为S-CO2的循环使用经济上没有吸引力。即使泵送功率非常小,液态金属或液态盐到S-CO2的间接循环也得出了类似的结论。这是因为需要增加中间液态金属(或液态盐)回路的额外成本,因为不可能将所有换热器放置在反应堆容器内进行再加热。

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