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Interpretation of Corrosion Mechanism on Cathode Side Separator for Molten Carbonate Fuel Cell

机译:熔融碳酸盐燃料电池阴极侧隔板腐蚀机理的解释

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摘要

This study was carried out for the purpose of investigating the corrOSIOn behavior and mechanism on a separator for a molten carbonate fuel cell under both the electrolyte and cathode side environment. A SUS310S austenitic stainless steel was used as the separator material. Corrosion proceeded via three steps; a formation step of corrosion product in which rapid corrosion take places until a stable corrosion product is formed after the beginning of corrosion; secondly, a protection step against corrosion until breakaway occurs after the formation step of the stable corrosion product; finally, an advance step of corrosion after breakaway. From the standpoint of the behavior of the elements in the separator, Fe, Cr and Ni were formed richly in the region of the corrosion product, in the region of corrosion protection, and at the Cr-depleted zone respectively. With respect to the corrosion mechanism, direct reaction with electrolyte and elements of the separator at the cathode side was the main corrosionmechanism, and the final corrosion product was LiFe02. The corrosion rate of the separator at the cathode side was rapid at the initial stage of corrosion.However, the corrosion rate was decreased due to the resistant effect of chromiumoxide.
机译:进行该研究的目的是研究在电解质和阴极侧环境下熔融碳酸盐燃料电池隔板上的腐蚀行为和机理。隔板材料使用SUS310S奥氏体不锈钢。腐蚀通过三个步骤进行:腐蚀产物的形成步骤,其中发生快速腐蚀,直到腐蚀开始后形成稳定的腐蚀产物为止;其次,在稳定的腐蚀产物的形成步骤之后,进行直到腐蚀发生的保护步骤。最后,分离后的腐蚀提前步骤。从隔板中元素的行为的观点来看,Fe,Cr和Ni分别在腐蚀产物区域,腐蚀防护区域和Cr贫化区富集。就腐蚀机理而言,与电解质和阴极侧隔板元素的直接反应是主要的腐蚀机理,最终腐蚀产物是LiFeO2。在腐蚀初期,隔板在阴极侧的腐蚀速率很快,但是由于氧化铬的抗腐蚀作用,腐蚀速率降低了。

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