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Analytical evaluation of heat sources and electrical resistance of a cermet electrode for the production of hydrogen in a membrane reactor

机译:膜反应器中用于制氢的金属陶瓷电极的热源和电阻的分析评估

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This work focuses on the calculation of transfers inside a cermet electrode for solid oxide membrane fuel cells and electrolysers for hydrogen production. A validation of the analytical model previously developed by our group for the calculation of transport quantities inside a cermet electrode was carried out. This model showed that the transport and transfer phenomena in the electrode are controlled by a new dimensionless number named A. This characteristic number is expressed with the parameters of the electrode and governs the repartition of the electrochemical reaction inside the volumetric electrode. The exploitation of this model was extended to predict heat sources and the effective electrical resistance in the membrane electrode in a direct manner and without numerical calculation. The results showed that the behaviour of these quantities follows two regimes: heat sources and the effective resistivity are dominated by the effects related to the electrochemical reaction for A 1, and by ohmic losses for A 1. The effective resistivity and heat sources are lower and less dependent on A in the ohmic regime. This means that increasing the electrochemical capabilities of the electrode, i.e the exchange current density and the density of the number of triple boundary points, along with decreasing the thickness of the electrolyte, is more beneficial than increasing the electrical conductivity of the solid oxide. This model provided guidelines and relevant orders of magnitude for the design of electrodes without using numerical calculation. Copyright (C) 2014, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:这项工作的重点是计算用于固体氧化物膜燃料电池的金属陶瓷电极和用于制氢的电解槽内的转移。对我们小组先前开发的用于计算金属陶瓷电极内部传输量的分析模型进行了验证。该模型表明,电极中的迁移和转移现象由名为A的新无量纲数控制。该特征数用电极的参数表示,并控制体积电极内部电化学反应的重新分配。该模型的开发被扩展为直接预测膜电极中的热源和有效电阻,而无需进行数值计算。结果表明,这些量的行为遵循两个机制:热源和有效电阻率受与A 1的电化学反应有关的影响和A 1的欧姆损耗的影响。有效电阻率和热量在欧姆状态下,源极低,对A的依赖性较小。这意味着增加电极的电化学性能,即交换电流密度和三重边界点数目的密度,以及减小电解质的厚度,比增加固体氧化物的电导率更有利。该模型无需使用数值计算即可为电极设计提供指导和相关的数量级。 Hydrogen Energy Publications,LLC版权所有(C)2014。由Elsevier Ltd.出版。保留所有权利。

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