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Performance of MIEC cathodes in SOFC stacks evaluated by means of FEM modeling

机译:通过FEM建模评估了SOFC堆栈中MiEC阴极的性能

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In planar solid oxide fuel cell (SOFC) stacks, anode supported cells are connected in series and in parallel by metal interconnectors (MIC), which always goes to the cost of performance. Further insight was gained with the help of a 2D-FEM repeat unit model, accounting for ohmic and polarisation losses on stack level. Implemented physical processes are i) gas diffusion in the porous electrodes, ii) electric/ionic conduction in the electrodes/electrolyte iii) and electrochemical electrode reactions. Material and kinetic parameters have been determined experimentally and the model is validated against measured data over a broad range of operating conditions. The 2D-FEM repeat unit model calculates performance in dependence on cathode dimensions, microstructure and chemical composition versus MIC-flowfield design. The calculations show, that performance is mainly limited by the oxidant gas transport underneath the contact rib for a given flowfield design. Thereby a well-chosen cathode thickness increases the overall power output of a planar SOFC stack most efficiently.
机译:在平面固体氧化物燃料电池(SOFC)堆叠中,阳极支撑的电池通过金属互连器(MIC)串联和并联连接,这始终达到性能成本。在2D-FEM重复单元模型的帮助下,获得了进一步的洞察力,占堆叠级别的欧姆和极化损失。实施物理过程是i)在多孔电极中的气体扩散,II)电极/电解质III的电/离子传导和电化学电极反应。已经通过实验确定了材料和动力学参数,并且在广泛的操作条件下验证了模型的测量数据。 2D-FEM重复单元模型根据阴极尺寸,微观结构和化学成分与MIC流场设计来计算性能。计算表明,该性能主要受给定流场设计的接触肋下方的氧化剂气体输送。因此,所选择的阴极厚度最有效地增加了平面SOFC堆的总功率输出。

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