Uptake of Ruthenium Bearing Waste by Co Precipitation using Lead Sulfide as Scavenger

B. Panigrahi
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Abstract

During the fission of Uranium for generating electricity, fission products are produced. Ru-106 is one among them. In the decontamination of nuclear components using decontaminating agents like EDTA, NDA, oxalic acid etc, Ruthenium gets complexed and the waste generated as liquid contains Ru-106 in the complex state. It is necessary to free Ru106 from the complex by oxidation of the complex. This will generate Ruthenium effluent with Ru-106 in the free state amenable for further treatment. An attempt has been made to co precipitate Ruthenium along with lead sulphide. The optimum pH, dosing of chemicals needed for in situ precipitation of lead sulphide were estimated in the batch study. Column studies using lead sulphide on polyurethane foam as column material were carried out for the treatment of Ruthenium bearing effluent. The optimum flow rate for maximum removal of Ruthenium was found to be 20 BV/h. Under optimized condition the max removal of Ruthenium was found to be 84% in the batch study, and 80% in the column study.
以硫化铅为清除剂的Co沉淀法吸收含钌废物
在铀裂变发电的过程中,会产生裂变产物。钌-106就是其中之一。在使用EDTA、NDA、草酸等去污剂对核部件进行去污时,钌发生络合,产生的废液中含有络合态的钌-106。必须通过络合物的氧化将钌106从络合物中分离出来。这将产生钌流出物,其中Ru-106处于可进一步处理的游离状态。人们曾尝试将钌与硫化铅一起共沉淀法。在批量研究中估计了原位沉淀硫化铅所需的最佳pH值和化学品的剂量。以聚氨酯泡沫上的硫化铅为柱材,对含钌废水进行了处理。钌的最佳去除率为20 BV/h。在优化的工艺条件下,批处理的最大钌去除率为84%,柱处理的最大钌去除率为80%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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