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Estimating Performance Degradation in Reformers for PAFC Power Plants by Using Increases in Steam-Reformed and Burner-Exhaust Gas Temperatures

机译:通过使用蒸汽重整和燃烧器排气温度的升高来估算PAFC电厂重整器的性能下降

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References(15) Cited-By(1) We simulated the performance degradation in a reformer for phosphoric-acid-fuel-cell (PAFC) power plants caused by deterioration of the catalyst loaded in the reformer. We found that the temperatures of the catalyst bed, steam-reformed gas, reformer-tube outer-wall, and burner-exhaust gas rise as the catalyst deteriorates. Increases in the steam-reformed and burner-exhaust gas temperatures at the reformer outlet proved to be the most useful parameters for estimating the drop in reformer performance caused by catalyst deterioration because they could be easily measured during power generation. These temperatures rise and the methane-conversion rate decreases as the catalyst deteriorates. By comparing the simulation results with measurements taken for a 200 kW PAFC power plant, we found that increases in the steam-reformed and burner-exhaust gas temperatures at the reformer outlet, instead of the methane-conversion rate, can be used as parameters for estimating the reformer-performance degradation, and that the steam-reformed-gas temperature is the better parameter of the two.
机译:参考文献(15)By-By(1)我们模拟了重整炉中由于装在重整炉中的催化剂的劣化而导致的磷酸燃料电池(PAFC)发电厂的性能下降。我们发现随着催化剂的劣化,催化剂床层,蒸汽重整气体,重整管外壁和燃烧器废气的温度升高。重整器出口处的蒸汽重整和燃烧器排气温度的升高被证明是最有效的参数,可用于估算由于催化剂变质而导致的重整器性能下降,因为在发电过程中很容易测量它们。随着催化剂的劣化,这些温度升高并且甲烷转化率降低。通过将模拟结果与对200 kW PAFC电厂进行的测量结果进行比较,我们发现重整器出口处的蒸汽重整和燃烧器废气温度的升高(而不是甲烷转化率)可以用作以下参数:估计重整器性能下降,并且蒸汽重整气体温度是两者中较好的参数。

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