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Simulation of start-up behaviour of a passive autocatalytic hydrogen recombiner

机译:仿真无源自催化氢重组器的启动行为

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摘要

Heterogeneous catalytic recombination of hydrogen with oxygen is one of the methods used to remove hydrogen from the containment of a light-water nuclear reactor (LWR). Inside a passive autocatalytic recombiner (PAR), hydrogen and oxygen molecules are adsorbed at catalyst active spots and they recombine to yield water. Heat released in this exothermic reaction creates natural convection of gas in the spaces between the elements supporting a catalyst. Hot and humid gas flows upwards into the PAR chimney, while fresh, hydrogen-rich gas enters the PAR from below. Catalytic recombination should start spontaneously at room temperature and low hydrogen concentration. Computational fluid dynamics (CFD) has been used to study the dynamic behaviour of a plate-type Areva FR-380 recombiner in a quiescent environment for several test scenarios, including different rates of increase in hydrogen concentration and temporary catalyst deactivation. A method for the determination of pressure boundary conditions at the PAR exits was proposed and implemented into a CFD code. In this way, transient operation of PAR could be simulated without the need to model gas circulation outside the device. It was found that first a slow downward flow of gas is developed, which may persist until the temperature of the catalyst foils rises. As soon as the gas inside the PAR absorbs enough heat to become lighter than the gas outside the PAR, it starts to flow upwards. Criteria for determining the start-up time of PAR were proposed. Model predictions were also compared with experimental data obtained in tests conducted at the THAI facility.
机译:用氧的氢的异质催化重组是用于从容纳轻水核反应堆(LWR)的氢气中除去氢的方法之一。在被动式自催化重组器(Par)内,氢气和氧分子在催化剂活性斑点上吸附并重新组合以产生水。在这种放热反应中释放的热量会在支撑催化剂的元件之间的空间中产生自然对流。热和潮湿的气体向上流入Par Chimney,而新鲜的富含氢气的气体从下面进入比率。催化重组应在室温下自发地开始,低氢浓度。计算流体动力学(CFD)已被用于研究板型ISVA FR-380重组器的动态行为,以进行几种测试场景,包括氢浓度的不同速率和临时催化剂失活的速率。提出了一种确定PAR退出处的压力边界条件的方法,并实施到CFD代码中。以这种方式,可以模拟PAR的瞬态操作而无需在装置外部的气体循环。发现首先开发出慢的气体流动,这可能持续,直到催化剂箔的温度升高。一旦气体内部的气体吸收足够的热量比标准板外的气体更轻,就开始向上流动。提出了确定比例的启动时间的标准。还将模型预测与在泰国设施的试验中获得的实验数据进行了比较。

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    Antoni Rożeń;

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  • 年度 2018
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  • 原文格式 PDF
  • 正文语种 eng
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