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HYDROGEN PRODUCTION USING HIGH-TEMPERATURE STEAM ELECTROLYSIS SUPPORTED BY ADVANCED GAS REACTORS WITH SUPERCRITICAL CO_2 CYCLES

机译:利用超临界CO_2循环高级气体反应器支持的高温蒸汽电解制氢

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Hydrogen production using high-temperature steam electrolysis (HTSE) supported by a supercritical CO_2 (SCO_2) recompression Brayton cycle that is directly coupled to an advanced gas-cooled reactor (AGR) is proposed in this paper. The system features and efficiency are analyzed in a parametric fashion. The analysis includes the influence of the major components' performance and the component integration in a proposed plant layout. The configuration, HTSE-SCO_2-AGR, with thermal recuperation from the product gas streams and an intermediate heat exchanger between the turbine exit and the feedwater stream is found to offer excellent thermal efficiency, operational flexibility, and expected cost. The HTSE average process temperature is 900℃, and the hydrogen pipeline delivery pressure is assumed to be 7 MPa for the evaluation of the plant performance. The reactor exit temperature and the SCO_2 cycle turbine inlet temperature are the same as those for the SCO_2 recompression cycle design: 550 to 700℃. The 900℃ at the HTSE unit, which is higher than the reactor exit temperature, is achieved with recuperative and electrical heating. HTSE is assumed to operate within 80 to 90% voltage efficiency at 1 atm to 7 MPa of pressure. A parametric analysis of these operating conditions shows that the system can achieve 38.6 to 48.2% low heating value of net hydrogen production energy efficiency. The extensive experience from commercial AGRs, the compactness of the SCO_2 power conversion system, and the progress in the electrolysis cell materials field can help the economical development of a future recuperative HTSE-SCO_2-AGR. The major research and development needs for this plant concept are materials processing for the durability and efficiency of the HTSE system, the design update of the AGR with advanced materials to resist high-pressure CO_2 coolant, thermal hydraulics of CO_2 at supercritical pressures, and detailed component design for system integration.
机译:本文提出了利用超临界CO_2(SCO_2)再压缩布雷顿循环与直接连接到先进气冷反应堆(AGR)的高温蒸汽电解(HTSE)来制氢。以参数方式分析系统功能和效率。该分析包括拟议的工厂布局中主要部件性能和部件集成的影响。 HTSE-SCO_2-AGR配置具有来自产品气流的热回收以及涡轮机出口和给水流之间的中间热交换器,可提供出色的热效率,操作灵活性和预期成本。 HTSE的平均过程温度为900℃,为评估工厂的性能,假定氢气管道的输送压力为7 MPa。反应器出口温度和SCO_2循环涡轮机入口温度与SCO_2再压缩循环设计的温度相同:550至700℃。通过换热和电加热,HTSE装置的900℃高于反应器出口温度。假设HTSE在1 atm至7 MPa的压力下可在80%至90%的电压效率内运行。对这些运行条件的参数分析表明,该系统可实现净氢生产能源效率的38.6%至48.2%的低发热量。商业AGR的广泛经验,SCO_2功率转换系统的紧凑性以及电解槽材料领域的进步可以帮助经济发展未来的回热式HTSE-SCO_2-AGR。该工厂概念的主要研发需求是:为提高HTSE系统的耐用性和效率而进行的材料处理,采用先进材料的AGR设计更新,以抵抗高压CO_2冷却剂,超临界压力下的CO_2热工学以及详细系统集成的组件设计。

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