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Electrochemical partitioning of actinides and rare earths in molten salt and cadmium solvents: Activity coefficients and equilibrium simulation.

机译:在熔融盐和镉溶剂中of系元素和稀土元素的电化学分配:活度系数和平衡模拟。

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The activity coefficients of actinide and rare earth chlorides in molten LiCl/KCl eutectic and of the reduced metals in molten cadmium have been calculated using a numerical method to minimize the Gibbs free energy. The generalized expansion by Wohl was used to express the concentration dependence of the excess Gibbs free energy. The activity coefficients were expressed in terms of the Wohl volume and interaction energy parameters. Laboratory tests of an electrochemical process for separating actinide metals from rare earth metals provide the experimental data. The Wohl parameters for the activity coefficients were obtained by minimizing the total Gibbs free energy.; A computer model was developed to simulate and predict results of laboratory electrorefining experiments. This model uses the activity coefficient expressions determined by free energy minimization in the equations for equilibrium to predict electrode potentials and solution concentrations in the process. Good agreement with experimental data has been found. The thermodynamic model will be useful for process design and scale-up calculations for separation processes.
机译:已使用数值方法计算了吉布斯自由能最小化,从而计算了熔融LiCl / KCl共晶中的act系元素和稀土氯化物的活度系数以及熔融镉中的还原金属的活度系数。 Wohl的广义扩展用于表示过量吉布斯自由能的浓度依赖性。活度系数用沃尔体积和相互作用能参数表示。从act金属中分离act系元素金属的电化学过程的实验室测试提供了实验数据。通过使总的吉布斯自由能最小化来获得活度系数的沃尔参数。开发了计算机模型来模拟和预测实验室电精炼实验的结果。该模型使用通过自由能最小化确定的平衡方程式中的活度系数表达式来预测过程中的电极电势和溶液浓度。已经发现与实验数据吻合良好。热力学模型将对分离过程的工艺设计和按比例放大计算有用。

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