作者: J Meusinger , E Riensche , U Stimming
DOI: 10.1016/S0378-7753(97)02763-8
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摘要: Internal steam reforming is an attractive option offering a significant cost reduction and higher system efficiencies of solid oxide fuel cell (SOFC) power plant. Furthermore, faster load response may characterise systems with internal reforming. However, complete can lead to several problems, which be avoided partial pre-reforming natural gas. For SOFC the ratio between has optimised on basis experimental performance data. A detailed study concerning in reformer considerable size (10 kW) carried out. The influence operating temperature mass flow variations conversion methane ethane analysed. During substrate anodes, large gradients were detected. Substrate samples low catalytic activity show times respect parameter variations.