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Recovery of deuterium from H-D gas mixture in thermal diffusion columns connected in series with countercurrent-flow transverse sampling streams

机译:在与逆流横向采样流串联连接的热扩散塔中从H-D气体混合物中回收氘

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The equations for predicting the degrees of separation of H-2, HD and D-2 from H-D gas mixture by thermal diffusion in countercurrent-flow concentric-tube Frazier schemes of single and multiple columns, have been derived. The equations for predicting the recovery of deuterium (D) in HD and D-2 were then obtained with the use of the atomic weight ratio. The degrees of separation, as well as separation factors, for deuterium recovery in the cryogenic-wall thermal diffusion devices were estimated, with the use of the experimental data obtained by Arita et al., 1998 and with the transport coefficients correlated in the previous work. Considerable improvement in deuterium recovery is achievable if a Frazier scheme with multiple columns is employed, instead of using the single-column device, either with the same column height, or with the same total sum of column heights, especially for the operation under larger volume flow rate and/or higher operating pressure. Further, countercurrent-flow operation is better than concurrent-flow operation in multi-column devices. (C) 2016 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:推导了单列和多列逆流同心管Frazier方案中通过热扩散从H-D气体混合物中分离H-2,HD和D-2的程度的方程。然后利用原子量比获得了预测HD和D-2中氘(D)回收率的方程式。利用Arita等人,1998年获得的实验数据以及先前工作中相关的迁移系数,估算了低温壁热扩散装置中氘回收的分离程度以及分离因子。 。如果采用具有多个色谱柱的Frazier方案,而不是使用具有相同色谱柱高度或相同色谱柱总高度的总和的单柱装置,则可以实现氘回收率的显着提高,特别是对于大体积操作流量和/或更高的工作压力。此外,在多柱装置中,逆流操作优于并流操作。 (C)2016氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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