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L_(0.8)Sr_(0.2)CoO_3 Coated Nickel Cathodes for Molten Carbonate Fuel Cells

机译:用于熔融碳酸盐燃料电池的L_(0.8)Sr_(0.2)CoO_3涂层镍阴极

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System efficiency and cost of the MCFC is advantageous when compared to other low temperature operating fuel cells. However, solubility of nickel oxide cathode in the electrolyte is one of the important problems facing the commercialization of MCFC technology. Nickel oxide reacts with the dissolved CO_2 in the electrolyte according to an acidic dissolution mechanism and dissolves in the molten carbonate during operation. The cation diffuses to the anode side of the electrolyte and is then reduced in the hydrogen atmosphere to metallic nickel. Precipitates of metallic nickel have been found in the electrolyte tile much closer to the anode and this precipitate acts as a sink for further deposition of nickel particles. This growth of the nickel layer eventually leads to a short circuit between the anode and cathode. The dissolution is accelerated under higher CO_2 partial pressure resulting in a decrease of the operating life of the cell. The dissolution of NiO also results in a decrease of the active surface area available for the oxygen reduction reaction resulting in degradation in the cell performance. More basic molten carbonate melts such as Li/Na carbonate eutectic does not favor the NiO dissolution process and have been used to decrease the Ni dissolution rate in the melt. Also, alkaline earth metal salts based on Ba or Sr have been used as additives to increase the basicity of the melt. However, using more basic molten carbonate melts only partially solves the problem, since these melts only decrease the NiO dissolution rate by 10 to 15%. The other approach to counter the nickel dissolution problem is to either modify NiO or to identify alternate cathode materials, which have longer life in the melt. Porous electrodes with good electronic conductivity, chemical stability and proper microstructure therefore offer the excellent choice for MCFC cathodes. Several ceramic materials with small solubility in the melt have been studied as alternatives to NiO. LiFeO_2, LiCoO_2~3 and La_(0.2)Sr_(0.8)CoO_3~4 offered initial promise as replacement material for NiO cathodes. LiCoO_2 coated nickel cathodes are reported in literature. Cobalt was coated mechanically onto nickel powder and used as the cathode. LiNiO_2 possess good conductivity and has been studied for high temperature applications. However, lithium loss occurs during heat treatment and the associated stoichiometry changes are undesirable. In this study, we have adopted the coating of La_(0.8)Sr_(0.2)CoO_3 perovskite material by a conventional sol-gel method onto the porous nickel electrodes.
机译:与其他低温运行的燃料电池相比,MCFC的系统效率和成本具有优势。然而,氧化镍阴极在电解质中的溶解度是MCFC技术商业化面临的重要问题之一。氧化镍根据酸性溶解机理与电解质中溶解的CO_2反应,并在操作过程中溶解在熔融碳酸盐中。阳离子扩散到电解质的阳极侧,然后在氢气氛中还原为金属镍。在更接近阳极的电解质砖中发现了金属镍的沉淀物,该沉淀物充当了镍颗粒进一步沉积的沉陷。镍层的这种生长最终导致阳极和阴极之间的短路。在较高的CO_2分压下会加速溶解,导致电池使用寿命降低。 NiO的溶解还导致可用于氧还原反应的活性表面积减少,从而导致电池性能下降。更多的碱性熔融碳酸盐熔体(例如Li / Na碳酸钠共晶)不利于NiO溶解过程,因此已被用来降低Ni在熔体中的溶解速率。同样,基于Ba或Sr的碱土金属盐已被用作添加剂以增加熔体的碱度。但是,使用更多的碱性熔融碳酸盐熔体只能部分解决该问题,因为这些熔体只会使NiO溶解率降低10%至15%。解决镍溶解问题的另一种方法是改性NiO或确定替代的阴极材料,这些材料在熔体中的寿命更长。因此,具有良好电导率,化学稳定性和适当微结构的多孔电极为MCFC阴极提供了绝佳的选择。已经研究了几种在熔体中具有低溶解度的陶瓷材料作为NiO的替代品。 LiFeO_2,LiCoO_2〜3和La_(0.2)Sr_(0.8)CoO_3〜4有望作为NiO阴极的替代材料。文献报道了LiCoO_2涂覆的镍阴极。将钴机械涂覆到镍粉上并用作阴极。 LiNiO_2具有良好的导电性,并已针对高温应用进行了研究。然而,锂的损失在热处理期间发生,并且相关的化学计量变化是不希望的。在这项研究中,我们通过常规的溶胶-凝胶法在多孔镍电极上采用了La_(0.8)Sr_(0.2)CoO_3钙钛矿材料的涂层。

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