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Column Separation of Am(III) and Eu(III) by α-Zirconium Phosphate Ion Exchanger in Nitric Acid

机译:氨基(III)和EU(III)的柱分离在硝酸中的α-锆磷酸锆离子交换剂

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The trivalent lanthanide-actinide separations are a major challenge in reprocessing ofnuclear fuels. To achieve this, commonly organic extractants and solvents are utilized in elaborateprocesses. Here we report a simple new method that can perform a supportive or alternative role.A nanocrystalline α-zirconium phosphate ion exchanger was utilized for Eu(III)/Am(III) columnseparation. Comprehensive preliminary studies were done using batch experiments to optimize thefinal separation conditions. The distribution coefficients for Eu were determined as a function ofpH (from 0 to 3) and salinity (Na, Sr). The distribution coefficients for Am were determined as afunction of pH, and Eu concentration, from 1:40 to 10,000:1 Eu:Am molar ratio. The exchanger alwayspreferred Eu over Am in our experimental conditions. Separation factors (Eu:Am) of up to 400 wereachieved in binary Eu-Am solution in pH 1. The breakthrough capacity was determined in dynamiccolumn conditions using Eu: 0.3 meq·g?1, which is approximately 4% of the theoretical maximumcapacity. Two types of hot column separation tests were conducted: (i) binary load (selective Amelution), and (ii) continuous equimolar binary feed. In both cases separation was achieved. In (i), themajority (82% of the recovered 93%) of Am could be purified from Eu with extremely high 99.999%molar purity, while alternatively even more (95% of the recovered 93%) at a lower purity of 99.7 mol%. In (ii), up to 330 L·kg?1 of the equimolar solution per mass of the exchanger could be treated withAm purity above 99.5 mol % in the total eluate. Alternatively, up to 630 L·kg?1 above 95 mol %, or upto 800 L·kg?1 above 90 mol % purities.
机译:三价镧系元素 - 贴滑动性分离是对核燃料再加工的主要挑战。为了实现这一点,在精美的过程中使用通常的有机萃取剂和溶剂。在这里,我们报告了一种简单的新方法,可以进行支持性或替代的作用。纳米晶α-磷酸锆离子交换剂用于EU(III)/ AM(III)柱。使用批量实验进行综合初步研究,以优化Final分离条件。欧盟的分布系数被确定为单击(0至3)和盐度(Na,Sr)的函数。 AM的分布系数被确定为pH和欧盟浓度的一定,从1:40至10,000:1 EU:AM摩尔比。交换机在我们的实验条件下始终如手欧盟。在pH1的二进制EU-AM溶液中,在二进制EU-AM溶液中产生的分离因子(EU:AM)高达400次突破的突破性容量使用EU:0.3 Meq·G?1,其约为理论最大程度的约4%。进行两种类型的热柱分离试验:(i)二元载荷(选择性Amelution),和(ii)连续等摩尔二进制饲料。在这两种情况下,达到了分离。在(i)中,可以从欧盟纯化摩尔纯度,摩尔纯度极高,同时较低纯度为99.7摩尔的较高纯度(95%回收的93%)的欧盟,同时均可纯化99.7摩尔的95%) %。在(ii)中,每块交换剂的等摩尔溶液的高达330升kgα1可以在总洗脱液中以高于99.5摩尔%的纯度处理。或者,高达630升·kg?1以上95摩尔%,或高达800升·kg?1以上90摩尔%纯度。

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