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Performance improvement of solid oxide fuel cell system using palladium membrane reactor with different operation modes

机译:使用不同运行模式的钯膜反应器改善固体氧化物燃料电池系统的性能

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The performance improvement of a solid oxide fuel cell (SOFC) system by replacing a conventional reformer with a palladium membrane reactor is investigated using 1D modeling. When pure hydrogen is extracted from the reaction mixture via the palladium membrane, the power density of the SOFC is improved, depending on the value of hydrogen recovery (ξ). Three operation modes of membrane reactors; i.e., high-pressure compressor (HPC-MR), combined low pressure compressor and vacuum pump (LPC-MR-V) and combined high-pressure compressor and vacuum pump (HPC-MR-V) are considered. Their overall SOFC system characteristics are compared with those of the SOFC system with the conventional reformer. The economic analysis reveals that the total capital costet electrical power is dependent on hydrogen recovery, net electrical efficiency and operation mode. At high electrical efficiency, the replacement of the conventional reformer with the membrane reactor becomes attractive. Finally, it is demonstrated that the HPC-MR-V is the best operation mode for integration with the SOFC system.
机译:使用一维模型研究了通过用钯膜反应器代替常规重整器来改善固体氧化物燃料电池(SOFC)系统的性能。当通过钯膜从反应混合物中提取纯氢时,SOFC的功率密度将提高,这取决于氢回收率(ξ)的值。膜反应器的三种运行模式;即,考虑了高压压缩机(HPC-MR),低压压缩机和真空泵的组合(LPC-MR-V)和高压压缩机和真空泵的组合(HPC-MR-V)。将它们的总体SOFC系统特性与使用常规重整器的SOFC系统的特性进行了比较。经济分析表明,总资本成本/净电功率取决于氢气回收率,净电效率和运行方式。在高电效率下,用膜反应器代替常规重整器变得有吸引力。最后,证明了HPC-MR-V是与SOFC系统集成的最佳操作模式。

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