LiCl-Li2O熔盐中U3O8的电化学还原及机理研究

    Electrochemical Reduction and Mechanistic of U3O8 in LiCl-Li2O Molten Salt

    • 摘要: 传统湿法后处理技术(如PUREX流程)存在废液生成量大、操作复杂等问题,而干法熔盐电解技术因其高效、废物量少等优势备受关注。通过干法熔盐电解技术将氧化物乏燃料转化为金属燃料是推动我国一体化快堆建设、实现闭式核燃料循环的关键环节。然而,我国在氧化物乏燃料电化学还原方面的研究报道较少,相关理论基础、实验方法及技术均相对薄弱。考虑到氧化物乏燃料中主要成分是UO2,在首端过程中UO2芯块通过氧化挥发技术转变为U3O8粉末。为此,本工作以U3O8固体粉末为对象,通过循环伏安法(CV)和恒电位电解实验,系统探究其在650 ℃的LiCl-Li2O熔盐中的电化学还原机理,并借助X射线衍射(XRD)、扫描电镜(SEM)及能谱分析(EDS)对电解产物的物相组成、微观形貌与元素分布进行表征。结果显示,电位扫描(1.50 V至0.00 V(vs. Li+/Li,下同))中观察到六个还原峰(c1—c6)及五个对应氧化峰(a1—a5),其中c1峰(0.00 V)为Li沉积,c2—c6峰(0.15−0.84 V)对应U3O8逐步还原为UO2和金属U的过程。恒电位电解实验显示在1.95 V下仅生成UO2相;1.20 V下产物为UO2与Li2UO4共存;而0.10~0.70 V未检测到金属U。这些结果表明U3O8电化学还原机理可能是:(1) 与Li+发生氧化还原反应生成UO2和Li2UO4;(2) Li2UO4进一步还原为UO2;(3) UO2逐步电脱氧形成U。脉冲式恒电压电解产物经XRD与SEM/EDS分析证实其中存在金属U和UO2,说明U3O8固体粉末在LiCl-Li2O熔盐体系中可直接电化学还原为金属U。通过直接氧化法测定,U3O8的平均还原率为45.47%,平均电流效率为22.86%。本研究阐明了U3O8在熔盐体系中的多步还原机制,揭示了关键中间产物的转化规律,为优化氧化物乏燃料电化学还原工艺参数(如电位控制、熔盐组分设计)提供了理论依据,对实现金属燃料的高效制备及核能可持续发展具有重要意义。

       

      Abstract: Traditional wet reprocessing technologies, such as the PUREX process, face challenges including high volumes of waste liquid generation and operational complexity. In contrast, dry reprocessing technology has garnered significant attention due to its high efficiency and reduced waste production. The conversion of spent oxide fuel into metallic fuel through dry reprocessing technology is a critical step in advancing the construction of integrated fast reactors in China and realizing a closed nuclear fuel cycle. However, few studies on the electrochemical reduction of oxide spent fuel have been reported in China, with relatively weak theoretical foundations, experimental methods, and associated technologies. Considering that the primary component of oxide spent fuel is UO2, UO2 pellets are converted into U3O8 powder via oxidation-volatilization techniques during the head-end process. Therefore this work focused on U3O8 solid powder, systematically investigating its electrochemical reduction mechanism in LiCl-Li2O molten salt at 650 ℃ through cyclic voltammetry(CV) and experiments of potentiostatic electrolysis. The phase composition, microstructure, and elemental distribution of electrolytic products were characterized using X-ray diffraction(XRD), scanning electron microscopy(SEM), and energy-dispersion spectroscopy(EDS). CV tests show that during the potential scan(1.50 V to 0.00 V vs. Li+/Li), six reduction peaks(c1-c6) and five corresponding oxidation peaks(a1-a5) are observed. The c1 peak(0.00 V) corresponds to Li deposition, while the c2-c6 peaks(0.15-0.84 V) are attributed to the stepwise reduction of U3O8 to UO2 and metallic uranium(U). Potentiostatic electrolysis experiment shows at 1.95 V(vs. Li+/Li), there is exclusively generated the UO2 phase. At 1.20 V, the products contain both UO2 and Li2UO4. However, no metallic U is detected at 0.70-0.10 V. These results indicate that the electrochemical reduction mechanism of U3O8 likely proceeds in three steps as following: (1) a redox reaction between U3O8 and Li+ to form UO2 and Li2UO4; (2) further electrochemical reduction of Li2UO4 to UO2; and (3) stepwise electro-deoxidation of UO2 to obtain metallic uranium(U). The presence of metallic U and UO2 in the products of pulsed constant-voltage electrolysis is confirmed by XRD and SEM/EDS analyses, demonstrating that U3O8 solid powder can be directly electrochemically reduced to metallic U in the system of LiCl-Li2O molten salt. Direct oxidation measurements reveal an average reduction rate of 45.47% for U3O8 and an average current efficiency of 22.86%. This work reveals the multi-step electrochemical reduction mechanism of U3O8 in LiCl-Li2O molten salt and uncovers the transformation pathways of key intermediates. These findings provide a theoretical basis for optimizing processes parameters in the electrochemical reduction of spent oxide fuels(e.g. potential control and molten salt composition design), offering significant implications for the efficient production of metallic fuels and the sustainable development of nuclear energy.

       

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