U(Ⅵ)电还原反萃动力学研究 Ⅰ.U(Ⅵ)电还原动力学

    STUDIES ON THE KINETICS OF U(Ⅵ) ELECTRO REDUCTION AND REEXTRACTION Ⅰ. KINETICS OF U(Ⅵ) ELECTRO REDUCTION

    • 摘要: 本文在带有阴阳极的恒界面池中研究了HNO_3-N_2H_5NO_3(H_2O)/UO_2(NO_3)_2-HNO_3(30%TBP-煤油)体系中U(Ⅵ)电还原动力学。这是U(Ⅵ)电还原反萃动力学研究的第一步。测定了两相溶液中各组分浓度对U(Ⅵ)电还原速率的影响。根据实验所得数据,经回归分析得到U(Ⅵ)电还原动力学微分方程: -(dU(Ⅵ)/dt)=kU(Ⅵ)_0~(1.294)HNO_3_0~(0.0143)HNO_3_α~(0.322)N_2H_5~+_α~(0.0178)式中k为速度常数,25℃时,k=1.816×10~(-4)。研究了阴极电位、操作温度、两相搅拌速率和界面面积对U(Ⅵ)电还原速率的影响。选定了公称实验条件,将U(Ⅵ)电还原速率与“比”实验条件进行关联,得到如下的经验方程: r=r_0E~(1.589)T~(0.155)W~(0.078)A~(0.265)式中r_0为公称实验条件下U(Ⅵ)电还原速率。在本文实验范围内,U(Ⅵ)电还原过程由电极反应控制。

       

      Abstract: The kinetics of U(Ⅵ) electro-reduction with the system of HNO3-N2H5NO3(H2O) /UO2(NO3)2-HN03 (30%TBP-OK) has been investigated. This is the first step of the investigation of the kinetics of U(Ⅵ) electro-reduction and reextraction. The experimental apparatus employed is a constant interfacial area cell (Lewis cell) with cathode and anode in it. The dependence of U(Ⅵ) electro-reduction rates on component concentrations in two phase solutions has been measured. According to the experimental data, a kinetics infinitesimal equation of U(Ⅵ) electro-reduction is given by.where k is rate constant, k= 1 .816×10-4 at t=25℃ The effect of the potential of cathode, the operating temperature, the stirring speed of two phases and the interfacial area between two phases on the U(Ⅵ) electro-reduction rates has also been investigated. The definition of the specific experimental conditions is introduced, the relation between the U(Ⅵ) electro-reduction rales and the specific experimental conditions is given by an empirical equation.where r0 is the U(Ⅵ) electro-reduction rate at the nominal experimental conditions. The process of U(Ⅵ) electro-reduction is mainly electrode reaction controlled.

       

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