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Numerical heat and mass transfer investigation of hydrogen absorption in an annulus-disc reactor

机译:圆盘反应器中氢吸收的数值传热与传质研究

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This work presents a numerical investigation of two-dimensional coupled heat and mass transfer process in a LaNi5-based annulus-disc reactor, during hydrogen absorption using the commercial software ANSYS-FLUENT 14.5. Temperature and amount of hydrogen absorbed and their averages inside the metal hydride bed are presented for different reactor design configurations and different cooling tube radii, respectively. Numerical simulations revealed that the pressure drop in the bed caused by fluid inertia may be considerable in this flow type, and the hydriding process time for the LaNi5 alloy depends on the configuration and geometrical dimensions of the tubular heat exchange device. Thus, the hydriding time minimization relates to the accommodation of the amount of heat removed from the bed reactor. A good agreement was found between the present computational results and the experimental data reported in the literature. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:这项工作提出了使用商业软件ANSYS-FLUENT 14.5在氢吸收过程中基于LaNi5的圆盘反应器中二维传热和传质过程的数值研究。分别针对不同的反应器设计配置和不同的冷却管半径,介绍了金属氢化物床内吸收的氢的温度和量及其平均值。数值模拟表明,在这种流动类型中,由流体惯性引起的床内压降可能很大,LaNi5合金的氢化过程时间取决于管状热交换装置的构造和几何尺寸。因此,最小化氢化时间涉及对从床反应器中除去的热量的调节。在当前的计算结果与文献报道的实验数据之间找到了很好的一致性。 Hydrogen Energy Publications,LLC版权所有(C)2015。由Elsevier Ltd.出版。保留所有权利。

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