首页> 外文会议>International conference on nuclear engineering;ICONE17 >SYSTEM ANALYSES OF HIGH AND LOW-TEMPERATURE INTERFACE DESIGNS FORA NUCLEAR-DRIVEN HIGH-TEMPERATURE ELECTROLYSIS HYDROGEN PRODUCTION PLANT
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SYSTEM ANALYSES OF HIGH AND LOW-TEMPERATURE INTERFACE DESIGNS FORA NUCLEAR-DRIVEN HIGH-TEMPERATURE ELECTROLYSIS HYDROGEN PRODUCTION PLANT

机译:核动力高温电解制氢厂的高温与低温界面设计的系统分析

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As part of the Next Generation Nuclear Plant (NGNP) project, an evaluation of a low-temperature heat-pump interface design for a nuclear-driven high-temperature electrolysis (HTE) hydrogen production plant was performed using the UniSim process analysis software. The low-temperature interface design is intended to reduce the interface temperature between the reactor power conversion system and the hydrogen production plant by extracting process heat from the low temperature portion of the power cycle rather than from the high-temperature portion of the cycle as is done with the current Idaho National Laboratory (INL) reference design. The intent of this design change is to mitigate the potential for tritium migration from the reactor core to the hydrogen plant, and reduce the potential for high temperature creep in the interface structures. The UniSim model assumed a 600 MW, Very-High Temperature Reactor (VHTR) operating at a primary system pressure of 7.0 MPa and a reactor outlet temperature of 900°C. The low-temperature heat-pump loop is a water/steam loop that operates between 2.6 MPa and 5.0 MPa. The HTE hydrogen production loop operated at 5 MPa, with plant conditions optimized to maximize plant performance (i.e., 800°C electrolysis operating temperature, area specific resistance (ASR) = 0.4 ohm-cm2, and a current density of 0.25 amps/cm2). An air sweep gas system was used to remove oxygen from the anode side of the electrolyzer. Heat was also recovered from the hydrogen and oxygen product streams to maximize hydrogen production efficiencies. The results of the UniSim analysis showed that the low-temperature interface design was an effective heat-pump concept, transferring 31.5 MW, from the low-temperature leg of the gas turbine power cycle to the HTE process boiler, while consuming 16.0 MW_e of compressor power. However, when this concept was compared with the current INL reference direct Brayton cycle design and with a modification of the reference design to simulate an indirect Brayton cycle (both with heat extracted from the high-temperature portion of the power cycle), thelatter two concepts had higher overall hydrogen production rates and efficiencies compared to the low-temperature heat-pump concept, but at the expense of higher interface temperatures. Therefore, the ultimate decision on the viability of the low-temperature heat-pump concept involves a tradeoff between the benefits of a lower-temperature interface between the power conversion system and the hydrogen production plant, and the reduced hydrogen production efficiency of the low-temperature heat-pump concept compared to concepts using high-temperature process heat.
机译:作为下一代核电站(NGNP)项目的一部分,使用UniSim工艺分析软件对核驱动高温电解(HTE)制氢厂的低温热泵接口设计进行了评估。低温接口设计旨在通过从功率循环的低温部分而不是从循环的高温部分提取过程热量来降低反应堆功率转换系统与制氢厂之间的接口温度。使用当前的爱达荷州国家实验室(INL)参考设计完成。这种设计更改的目的是减轻tri从反应堆堆芯迁移到制氢厂的可能性,并减少界面结构中高温蠕变的可能性。 UniSim模型假定一个600 MW的超高温反应堆(VHTR)在7.0 MPa的主系统压力和900°C的反应堆出口温度下运行。低温热泵回路是在2.6 MPa和5.0 MPa之间运行的水/蒸汽回路。 HTE制氢回路的运行压力为5 MPa,优化了工厂条件以最大限度地提高工厂性能(即800°C电解操作温度,面积比电阻(ASR)= 0.4 ohm-cm2,电流密度为0.25安培/ cm2) 。使用空气吹扫气系统从电解器的阳极侧除去氧气。还从氢气和氧气产物流中回收热量,以最大程度地提高氢气生产效率。 UniSim分析的结果表明,低温接口设计是有效的热泵概念,将31.5 MW从燃气轮机功率循环的低温段传递到HTE工艺锅炉,同时消耗16.0 MW_e的压缩机力量。但是,将此概念与当前的INL参考直接布雷顿循环设计以及对参考设计的修改进行比较以模拟间接布雷顿循环(两者均从功率循环高温部分提取的热量)进行比较时, 与低温热泵概念相比,后两个概念具有更高的总氢气产生速率和效率,但以更高的界面温度为代价。因此,关于低温热泵概念可行性的最终决定包括权衡功率转换系统和制氢厂之间的低温接口所带来的好处,以及降低低热泵概念的制氢效率。温度热泵概念与使用高温过程热的概念相比。

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