Recovery of uranium from conversion production sludge by leaching with nitric acid and subsequent ion-exchange concentration

IF 4.8 2区 材料科学 Q1 METALLURGY & METALLURGICAL ENGINEERING
Sergey Yu Skripchenko , Ksenia A. Nalivaiko , Svetlana M. Titova , Vladimir N. Rychkov , Vladimir S. Semenishchev
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Abstract

Physicochemical studies of the sludge of uranium conversion production were carried out to determine the possibility of its processing and return of uranium to the nuclear fuel cycle. It has been established that the sludge was mainly represented by calcium compounds: CaSO4·2H2O (60.1 wt%), CaCO3 (25.1 wt%), CaF2 (13.7 wt%), and silicon dioxide (1.2 wt%). The content of uranium in the sludge was 0.15 wt%. It was shown that it was possible to achieve high degrees of uranium extraction from the sludge using nitric acid as a leaching agent. The use of phosphorus-containing ion-exchanger Tulsion CH93 ensured the effective concentration of uranium from highly acidic pregnant leach solutions. The full dynamic exchange capacity achieved 15.7 kg m−3. The degree of uranium desorption by ACBM (ammonium carbonate/bicarbonate mixture) solutions was 83%. The final product was ammonium uranyl phosphate hydrate NH4UO2PO4∙3H2O with a uranium content of 52.5 wt%.

Abstract Image

Abstract Image

通过硝酸浸出和随后的离子交换浓缩从转化生产污泥中回收铀
对铀转化生产污泥进行了物理化学研究,以确定对其进行处理并将铀返回核燃料循环的可能性。研究发现,污泥中主要是钙化合物:CaSO4-2H2O(60.1%)、CaCO3(25.1%)、CaF2(13.7%)和二氧化硅(1.2%)。污泥中的铀含量为 0.15 wt%。研究表明,使用硝酸作为浸出剂,可以实现从污泥中高度提取铀。含磷离子交换剂 Tulsion CH93 的使用确保了高酸性孕浸溶液中铀的有效浓缩。全动态交换容量达到 15.7 kg m-3。ACBM (碳酸铵/碳酸氢铵混合物)溶液的铀解吸率为 83%。最终产品为水合铀酰磷酸铵 NH4UO2PO4∙3H2O,铀含量为 52.5 wt%。
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来源期刊
Hydrometallurgy
Hydrometallurgy 工程技术-冶金工程
CiteScore
9.50
自引率
6.40%
发文量
144
审稿时长
3.4 months
期刊介绍: Hydrometallurgy aims to compile studies on novel processes, process design, chemistry, modelling, control, economics and interfaces between unit operations, and to provide a forum for discussions on case histories and operational difficulties. Topics covered include: leaching of metal values by chemical reagents or bacterial action at ambient or elevated pressures and temperatures; separation of solids from leach liquors; removal of impurities and recovery of metal values by precipitation, ion exchange, solvent extraction, gaseous reduction, cementation, electro-winning and electro-refining; pre-treatment of ores by roasting or chemical treatments such as halogenation or reduction; recycling of reagents and treatment of effluents.
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