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Salt clean-up for recycling by electrolysis with a cathode-perforated ceramic container assembly

机译:用阴极穿孔的陶瓷容器组件通过电解进行盐回收净化

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摘要

Pyroprocessing is a promising way for the recovery of actinide elements from the used nuclear fuel. Electro-refining is a key technology of pyroprocessing and the electro-refining is generally composed of two recovery steps - deposit of uranium onto a solid cathode and the recovery of actinide elements by a liquid cathode. After the electro-refining process, it is necessary to remove the solutes from the molten salt for the salt regeneration. In this study, it was attempted to clean up a molten salt with a solid cathode- perforated ceramic container assembly and a glassy carbon anode. LiCl-KCl eutectic salt was used as a medium of the electrolytic bath. Uranium and cerium were used as solutes, where uranium was used as a surrogate for the actinide elements. The initial contents of uranium and cerium in the salt were varied in the range of 0-5 wt%. Electrolysis experiments were carried out by passing a constant current between the anode and cathode at 500 C. The solute contents were measured using ICP-AES spectroscopy. The initial cathode potential was about -1.6 V. This value decreased with increasing time in the salt. The solutes in the saline phase were successfully recovered onto the cathode.
机译:热解法是一种从用过的核燃料中回收of系元素的有前途的方法。电精制是高温处理的一项关键技术,电精制通常包括两个回收步骤-将铀沉积到固体阴极上以及通过液体阴极回收act系元素。在电精制过程之后,有必要从熔融盐中去除溶质以进行盐再生。在这项研究中,尝试使用带固体阴极穿孔的陶瓷容器组件和玻璃碳阳极来清理熔融盐。 LiCl-KCl低共熔盐用作电解浴的介质。铀和铈用作溶质,其中铀用作act系元素的替代物。盐中铀和铈的初始含量在0-5 wt%的范围内变化。通过在500°C下在阳极和阴极之间通过恒定电流进行电解实验。使用ICP-AES光谱法测量溶质含量。初始阴极电势约为-1.6V。该值随着盐中时间的增加而降低。将盐相中的溶质成功地回收到阴极上。

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