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Effects of structural and concentration polarization on the efficiency of Pd membrane permeator

机译:结构极化和浓度极化对Pd膜渗透器效率的影响

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For the processes of extracting hydrogen from the mixed gas of fusion reactors, it is of benefit to find an efficient method for hydrogen isotopes recovery and cyclic utilization. To enhance the hydrogen extraction efficiency, the properties of hydrogen permeation under various operating conditions in the tubular Pd membrane reactor system have been first investigated using the computational fluid dynamics (CFD) and material diffusion model. The results show that the predominated factor for the hydrogen extraction efficiency of tubular Pd membrane reactor is the fluid field of permeation pipe, further the effects of flux velocity, membrane length and thickness on the extraction efficiency at different pressures, as well as the concentration polarization effect at different conditions have been evaluated. The results could be significant for improving the engineering design of a highly efficient extraction Pd reactor by greater aspect ratio reactor. In addition, this method can also be used to simulate isotope separation process in Pd membrane reactor.
机译:对于从聚变反应堆混合气体中提取氢气的过程,寻找一种有效的氢同位素回收和循环利用方法是有益的。为了提高氢气的提取效率,首先使用计算流体力学(CFD)和材料扩散模型研究了管状Pd膜反应器系统中各种操作条件下氢气的渗透性能。结果表明,管式Pd膜反应器的氢萃取效率的主要影响因素是渗透管的流场,以及通量,膜长和膜厚对不同压力下萃取效率以及浓度极化的影响。已经评估了在不同条件下的效果。该结果对于通过更大纵横比的反应器改进高效萃取Pd反应器的工程设计可能具有重要意义。此外,该方法还可用于模拟钯膜反应器中同位素的分离过程。

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