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Extraction and stripping of actinide elements with changes in supply flow rate and nitric acid concentration using centrifugal contactors in single cycle solvent extraction system

机译:使用单循环溶剂萃取系统中的离心接触器,通过改变供应流速和硝酸浓度来萃取和脱除act系元素

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Counter current experiments in a single cycle solvent extraction system were carried out with centrifugal contactors to study flow rate reductions in extraction solvent and stripping solution with a dissolver solution of irradiated mixed oxide (MOX) fuel. Uranium and Pu leaked to the raffinate with a 15% decrease in the extraction solvent flow rate, which brought about an accumulation of U and Pu in the co-decontamination section. The discharge of other actinide elements and fission products (FPs) in the raffinate was constant when the extraction solvent reduced by 15%. On the other hand, a 15% decrease in the stripping solution flow rate did not affect the stripping of U and Pu so greatly. The polymerization of Pu was not observed in the counter current experiments, and the time taken to change 2% of Pu(IV) to Pu polymers in the stripping section was evaluated. Simulation results based on these experiments showed that a high HNO3 concentration in the feed solution was advantageous for Np extraction, because Np oxidation progressed in the extraction section.
机译:使用离心接触器在单循环溶剂萃取系统中进行逆流实验,以研究萃取溶剂和汽提溶液在辐照混合氧化物(MOX)燃料溶解器中的流速降低情况。铀和Pu泄漏到萃余液中,萃取溶剂流速降低了15%,这导致了U和Pu在共净化段中的积累。当萃取溶剂减少15%时,萃余液中其他act系元素和裂变产物(FPs)的排放是恒定的。另一方面,汽提溶液流速降低15%并没有太大地影响U和Pu的汽提。在逆流实验中未观察到Pu的聚合反应,并评估了在汽提段中将2%的Pu(IV)转变为Pu聚合物所花费的时间。基于这些实验的模拟结果表明,进料溶液中高浓度的HNO3有利于Np的提取,因为Np的氧化在提取区进行。

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