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    碱性电解水NiMo阴极的衰减机理研究

    Degradation mechanism of NiMo cathodes in alkaline water electrolysis

    • 摘要: 为了揭示碱性电解水镍基阴极在极端极化工况下的性能演化规律与失效机制,采用大气等离子喷涂制备NiMo合金催化电极。依托单小室电解槽平台,系统开展极限电流(250010000 A/m2)、电源波动(高频启停与反向电流)及杂质(Cr/Cl)协同毒化等多重极端加速应力测试,定量剖析其微观形貌坍塌与物相晶格重构特征。结果表明,在稳态高负荷运行下,极高产气率引发湍流,高频气泡动力学产生强烈的界面流体力学剪切应力,直接致使催化层发生微裂纹扩展与大面积脆性物理剥落;电流升至10000 A/m2时,核心活性元素Mo质量分数由6.97%骤降至1.07%,导致催化位点严重流失。在频繁启停与反向极化冲击中,高压氧化电场驱动Mo发生选择性电化学溶解,并诱导基底发生深度晶格重构,不可逆转化为致密且高势垒的惰性β-Ni(OH)2及高价γ-NiOOH相。该深度钝化严重迟滞反应动力学,致使Tafel斜率由48.56 mV急剧攀升至120.36 mV。杂质测试证实,Cl击穿表面钝化膜并加速Mo溶出,其引发的点蚀缺陷随即成为Cr物种沉积的优先成核点,二者结合形成的绝缘层引发强烈的协同毒化与封堵效应。深层机制指出,阴极最终失效是由机械物理剥离、化学钝化腐蚀与杂质协同毒化三大机制深度耦合所致;涂层机械结合稳定性不足制约大电流连续运行,而电位波动引发的晶格相变失活与杂质高强度沉积则全面主导非稳态工况下的加速致损过程。

       

      Abstract: To reveal the performance evolution behaviors and failure mechanisms of nickel-based cathodes for alkaline water electrolysis under extreme polarization conditions, NiMo alloy catalytic electrodes were prepared via atmospheric plasma spraying in this study. Relying on a single-cell electrolyzer platform, multiple extreme accelerated stress tests-including extreme current densities (250010000 A/m2), power fluctuations (high-frequency start-stop cycles and reverse current), and impurity (Cr/Cl) synergistic poisoning—were systematically conducted to quantitatively analyze their microstructural collapse and phase lattice reconstruction characteristics. The results indicate that under steady-state high-load operation, the extremely high gas evolution rate triggers turbulence, and high-frequency bubble dynamics generate strong interfacial hydrodynamic shear stress, which directly causes microcrack propagation and large-scale brittle physical spalling of the catalytic layer. When the current density increases to 10000 A/m2, the mass fraction of the core active element Mo drops sharply from 6.97% to 1.07%, leading to a severe loss of catalytic sites. Under frequent start-stop and reverse polarization impacts, the high-voltage oxidizing electric field drives the selective electrochemical dissolution of Mo and induces deep lattice reconstruction of the substrate, irreversibly transforming it into dense, high-barrier, and inert β-Ni(OH)2 and high-valence γ-NiOOH phases. This deep passivation severely retards the reaction kinetics, causing the Tafel slope to increase sharply from 48.56 mV to 120.36 mV. Furthermore, impurity tests confirm that Cl penetrates the surface passivation film and accelerates Mo dissolution. The resulting pitting defects then act as preferential nucleation sites for the deposition of Cr species, and the insulating layer formed by their combination triggers strong synergistic poisoning and pore-blocking effects. The underlying mechanisms indicate that the ultimate failure of the cathode is caused by the deep coupling of three major mechanisms: mechanical physical spalling, chemical passivation corrosion, and synergistic impurity poisoning. The insufficient mechanical binding stability of the coating restricts continuous operation at high currents, whereas lattice phase transition deactivation and high-intensity impurity deposition induced by potential fluctuations fully dominate the accelerated damage process under non-steady-state conditions.

       

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