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DEVELOPMENT OF TREATMENT PROCESS FOR ANODE RESIDUE FROM MOLTEN SALT ELECTROREFINING OF SPENT METALLIC FAST REACTOR FUEL

机译:速成金属快速反应釜熔融盐电解精制阳极残渣的处理工艺开发

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摘要

A new treatment process was proposed for the anode residue from a molten salt electrorefining step in the pyrometallurgical reprocessing of spent metallic fast reactor fuel. This treatment process consists of two steps: (a) oxidation of the remaining actinides in the anode residue by the addition of CdCl2 and (b) removal of the accompanying chloride by high-temperature distillation. The oxidation of the remaining uranium by CdCl2 was studied using anode residue from previous electrorefining experiments using U-Zr alloys. The reaction between uranium and CdCl2 was completed in ~2 days with a satisfactory chlorine balance among the species in the molten chlorides solvent. A high uranium oxidation rate was attained by appropriately controlling the rate of CdCl2 addition. The high-temperature distillation tests were carried out at 1473 K with pressure of ~300 Pa to remove the solvent accompanying the anode residue. The chloride content in the anode residue was lowered to 1% to 2.5% by the distillation operation. Although the anode residue was heated to 1673 to 1773 K at a pressure of ~50 kPa after the distillation, it was not melted completely. The remaining ratio of uranium after the electrorefining and the above treatment process was evaluated to be 0.04% to 0.20%. Material flow calculations were performed for a pyrometallurgical reprocessing facility equipped with the anode residue treatment process. It showed that (a) the chlorine and uranium supply/demand balance is maintained unless the remaining ratio of uranium after electrorefining exceeds a certain value and (b) the addition of the anode residue treatment process does not have an adverse effect on either the performance of the overall process or the facility design.
机译:针对乏金属快堆燃料的火法冶金后处理,提出了一种用于熔融盐电精制步骤中阳极残渣的新处理方法。该处理过程包括两个步骤:(a)通过添加CdCl2氧化阳极残留物中剩余的act系元素,以及(b)通过高温蒸馏去除伴随的氯化物。使用以前的使用U-Zr合金进行电精炼实验的阳极残渣研究了CdCl2对剩余铀的氧化。铀与CdCl2之间的反应在约2天内完成,熔融氯化物溶剂中的各种物种之间的氯平衡令人满意。通过适当地控制CdCl 2的添加速率,可以获得高的铀氧化速率。高温蒸馏试验在1473 K〜300 Pa的压力下进行,以除去伴随阳极残渣的溶剂。通过蒸馏操作将阳极残余物中的氯含量降低至1%至2.5%。尽管在蒸馏后将阳极残渣在〜50 kPa的压力下加热到1673至1773 K,但它并未完全熔化。在电精制和上述处理过程之后,铀的剩余比率被评估为0.04%至0.20%。对装备有阳极残渣处理工艺的火法冶金后处理设施进行了物料流量计算。结果表明:(a)除非电精炼后铀的剩余比率超过一定值,否则将维持氯和铀的供需平衡;(b)添加阳极残渣处理工艺不会对两者的性能产生不利影响整个过程或设施设计。

著录项

  • 来源
    《Nuclear Technology》 |2013年第3期|507-525|共19页
  • 作者单位

    Central Research Institute of Electric Power Industry, Nuclear Technology Research Laboratory, 2-11-1 Iwado-kita, Komae-shi, Tokyo 201-8511, Japan;

    Central Research Institute of Electric Power Industry, Nuclear Technology Research Laboratory, 2-11-1 Iwado-kita, Komae-shi, Tokyo 201-8511, Japan;

    Central Research Institute of Electric Power Industry, Nuclear Technology Research Laboratory, 2-11-1 Iwado-kita, Komae-shi, Tokyo 201-8511, Japan;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    pyrometallurgical reprocessing; electrorefining; high temperature distillation;

    机译:火法冶金后处理;电精炼;高温蒸馏;
  • 入库时间 2022-08-18 00:43:16

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