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A design study for tritium recovery system from cooling water of a fusion power plant

机译:聚变电厂冷却水recovery回收系统的设计研究

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Several systems for the tritium recovery from cooling water of a blanket of a fusion power plant have been designed. The tritium concentration in the cooling water and the tritium permeation rate to the coolant is assumed to be 370 GBq(10Ci)/kg, 13 and 130g/day, respectively. For the case of 13g/day, the system can be composed of a water distillation (WD: 2.6m inner diameter and ~50 m height) and a catalytic exchange column with an electrolysis cell (0.7 m inner diameter and 22 m in height). The WD column can be replaced by a system of catalytic exchange columns in vapor and liquid phases. For the case of 130 g/day, no solution can be found as long as quite a large flow rate to a main fuel cycle for its final treatment is permitted. Otherwise, an electrolysis cell that can be used under a high concentration of tritium water will need to be developed. The tritium inventory of the WD column is appreciably large, so that it is desirable to develop a system having a high separation factor and with no liquid phase.
机译:已经设计了几种用于从聚变电站的毯子的冷却水中回收t的系统。假设冷却水中的t浓度和冷却剂中的tri渗透率分别为370 GBq(10Ci)/ kg,13和130g /天。对于每天13g的系统,该系统可由水蒸馏(WD:内径2.6m,高度约50m)和带有电解池(内径0.7m,高22m)的催化交换塔组成。 。 WD色谱柱可用气相和液相催化交换柱系统代替。对于130克/天的情况,只要允许对主燃料循环进行最终处理的流量很大,就找不到任何解决方案。否则,将需要开发可在高浓度water水下使用的电解槽。 WD塔的inventory存量相当大,因此希望开发一种分离系数高且没有液相的系统。

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