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Electrolytic Oxidation of Ce(III) to Ce(IV) in Nitric Acid Solution and Separation of Ce(IV) by Anion Exchange Method

机译:硝酸溶液中Ce(III)电解氧化为Ce(IV)并通过阴离子交换法分离Ce(IV)

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To develop an efficient method to recover Ce from radioactive wastes containing concentrated nitric acid, we have studied the possibility of the combination methods of selective electro-oxidation and anion exchange. The redox reaction behavior of Ce(IV)/Ce(III) in nitric acid solution has been investigated. Anion exchange behavior of Ce(IV) at various nitric acid concentrations and temperatures was studied. Moreover, separation of Ce(IV) from other rare earth elements was attempted by anion exchanger column. The results of study by cyclic voltammetry indicate that the kinetics of the Ce(IV)/Ce(III) redox reaction on carbon electrode was significantly promoted by increasing HNO_3 concentration, while the formal redox potential remained at almost constant values between 1.34- 1.38V(vs.Ag/AgCl). Electrolytic oxidation of Ce(III) to Ce(IV) in 6 mol centre dot dm~(-3) HNO_3 solution was successfully performed with the conversion of 100 percent and current efficiency near 60 percent by using a novel flow type electrolysis cell containing a carbon-fiber column electrode as working electrode and Vycor Glass(porous silica glass) as separator. Ce(IV) showed relatively strong adsorption on AR-0l anion exchanger as the form of nitrato-complexes such as Ce(NO_3)_5~- and Ce(NO_3)_6~(2-) and the distribution coefficient increased with increasing HNO_3 concentration. However, the adsorbed Ce(IV) was reduced to Ce(III) and eluted into the solution through redox reaction with the anion exchanger. Lowering temperature (<288 K) can considerably suppress the redox reaction between Ce(IV) and the anion exchanger. It was found that the separation factor between Ce(IV) and other trivalent rare earths at 278 - 288K was as high as 25 - 60. Separation experiments by AR-0l packed column demonstrated that Ce can be separated with high purity from a nitric acid solution containing La(III), Ce(III) and Nd(III) after electro-oxidation using the flow type electrolysis cell. The recovery of Ce was 82 percent at 278 K, while La and Nd were not detected in the recovered Ce product solution.
机译:为了开发一种从含有浓硝酸的放射性废物中回收铈的有效方法,我们研究了选择性电氧化和阴离子交换相结合的方法的可能性。研究了Ce(IV)/ Ce(III)在硝酸溶液中的氧化还原反应行为。研究了不同硝酸浓度和温度下Ce(IV)的阴离子交换行为。此外,尝试通过阴离子交换柱将Ce(IV)与其他稀土元素分离。循环伏安法的研究结果表明,通过增加HNO_3浓度,碳电极上Ce(IV)/ Ce(III)氧化还原反应的动力学得到了显着促进,而形式氧化还原电势则保持在1.34-1.38V的几乎恒定值(相对于Ag / AgCl)。通过使用新型的流式电解池,在6 mol中心点dm〜(-3)HNO_3溶液中成功地将Ce(III)电解氧化为Ce(IV),转化率为100%,电流效率接近60%。碳纤维柱电极为工作电极,Vycor玻璃(多孔石英玻璃)为隔板。 Ce(IV)以硝酸盐络合物的形式存在于AR-0l阴离子交换剂上,吸附强度相对较高,例如Ce(NO_3)_5〜-和Ce(NO_3)_6〜(2-)等,其分布系数随HNO_3浓度的增加而增加。但是,吸附的Ce(IV)还原为Ce(III),并通过与阴离子交换剂的氧化还原反应洗脱到溶液中。降低温度(<288 K)可以大大抑制Ce(IV)与阴离子交换剂之间的氧化还原反应。发现在278-288K时Ce(IV)与其他三价稀土之间的分离系数高达25-60。AR-0l填充柱的分离实验表明,可以从硝酸中分离出高纯度的Ce。使用流动式电解池进行电氧化后,生成包含La(III),Ce(III)和Nd(III)的溶液。在278 K下Ce的回收率为82%,而在回收的Ce产品溶液中未检测到La和Nd。

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