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URANIUM TRANSPORT IN A HIGH-THROUGHPUT ELECTROREFINER FOR EBR-II BLANKET FUEL

机译:用于EBR-II毛毯燃料的高通量电精炼炉中的铀运输

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A unique high-throughput Mk-V electrorefiner is being used in the electrometallurgical treatment of the metallic sodium-bonded blanket fuel from the Experimental Breeder Reactor II. Over many cycles, it transports uranium back and forth between the anodic fuel dissolution baskets and the cathode tubes until, because of imperfect adherence of the dendrites, it all ends up in the product collector at the bottom. The transport behavior of uranium in the high-throughput electrorefiner can be understood in terms of the sticking coefficients for uranium adherence to the cathode tubes in the forward direction and to the dissolution baskets in the reverse direction. The sticking coefficients are inferred from the experimental voltage and current traces and are correlated in terms of a single parameter representing the ratio of the cell current to the limiting current at the surface acting as the cathode. The correlations are incorporated into an engineering model that calculates the transport of uranium in the different modes of operation. The model also uses the experimentally derived electrorefiner operating maps that describe the relationship between the cell voltage and the cell current for the three principal transport modes. It is shown that the model correctly simulates the cycle-to-cycle variation of the voltage and current profiles. The model is used to conduct a parametric study of electrorefiner throughput rate as a function of the principal operating parameters. The throughput rate is found to improve with lowering of the basket rotation speed, reduction of UCl_3 concentration in salt, and increasing the maximum cell current or cut-off voltage. Operating conditions are identified that can improve the throughput rate by 60 to 70% over that achieved at present.
机译:独特的高通量Mk-V电精炼机正用于对实验性增殖反应堆II的金属钠键合毯状燃料进行电冶金处理。在许多循环中,它在阳极燃料溶解篮和阴极管之间来回运输铀,直到由于树枝状晶体的不完美附着,所有铀最终都到达底部的产品收集器中。铀在高通量电精制机中的传输行为可以通过铀在正方向上粘附到阴极管以及在反方向上粘附到溶出篮的粘附系数来理解。粘着系数是从实验电压和电流迹线推断出的,并根据单个参数进行关联,该参数代表电池电流与充当阴极的表面上的极限电流之比。相关性被并入到工程模型中,该工程模型计算了不同操作模式下的铀迁移率。该模型还使用实验得出的电精炼器操作图,该图描述了三种主要传输模式下电池电压和电池电流之间的关系。结果表明,该模型正确地模拟了电压和电流曲线的逐周期变化。该模型用于根据主要操作参数进行电精炼机吞吐率的参数研究。发现吞吐速率随着篮筐转速的降低,盐中UCl_3浓度的降低以及最大电池电流或截止电压的提高而提高。确定了可以使吞吐率比目前提高60%到70%的操作条件。

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