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Operational experience with the JET AGHS cryodistillation system during and after DTE1

机译:在DTE1期间和之后使用JET AGHS低温蒸馏系统的操作经验

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The JET Active Gas Handing (AGH) Cryodistillation system (CD) was designed to separate a mixture of hydrogen isotopes into individual isotopic components, discharging low activity protium gas directly to stack, and storing the deuterium and tritium product for re-use. Following successful trace tritium commissioning the system became fully operational for the JET DTE1 experimental campaign which commenced in 1997. This paper describes the operating performance of the CD system during and after this period. This includes an assessment of the total amount of gas processed and the operating conditions which were implemented to achieve optimum process conditions. Note that the original design specification of the system assumed a large proportion of process gas would be protium from the fast pellet injection system. This system was not used during the campaign and consequently the feed gas was mainly a deuterium mix requiring the discharge of large amounts of detritiated deuterium to stack. Hence operating parameters had to be changed to suit these new conditions, which led to a need to keep the tritium inventory in the system to a minimum. Despite this, the overall tritium enrichment in the system with a feed of low activity hydrogen input was up to 35 thus providing an effective pre-enrichment level for introduction to the preparative Gas Chromatograph (GC) hydrogen isotope separation system used in the AGHS. In this respect even though the operational requirements of CD had changed from the original design specification, the system was successfully adapted to its revised ro
机译:JET活性气体处理(AGH)低温蒸馏系统(CD)旨在将氢同位素的混合物分离成单独的同位素组分,将低活度的gas气直接排放到堆中,并存储氘和tri产品以供再次使用。在成功进行痕量tri调试之后,该系统已为1997年开始的JET DTE1实验活动全面投入使用。本文介绍了CD系统在此期间及之后的运行性能。这包括对已处理气体总量和为实现最佳工艺条件而实施的操作条件的评估。请注意,该系统的原始设计规格假设来自快速粒料注入系统的大部分工艺气体为pro。在战役期间未使用该系统,因此原料气主要是氘混合物,需要排放大量堆积的氘。因此,必须改变操作参数以适应这些新条件,这导致需要将系统中的inventory存量保持在最低水平。尽管如此,使用低活性氢输入进料的系统中总tri富集量高达35,因此为引入用于AGHS的制备型气相色谱(GC)氢同位素分离系统提供了有效的预富集水平。在这方面,即使CD的操作要求已从原始设计规范中更改,该系统仍已成功地适应其修订的RO

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