期刊
FUEL CELLS
卷 8, 期 1, 页码 62-68出版社
WILEY-V C H VERLAG GMBH
DOI: 10.1002/fuce.200700018
关键词
ethanol steam reforming; hydrogen production; membrane reactor; Pd dense membrane; PEMFC
In this work, the ethanol steam reforming (ESR) reaction has been studied by using a dense Pd-Ag membrane reactor (MR) by varying the water/ethanol molar ratio between 3:1 and 9:1 in a temperature range of 300-400 C and at 1.3 bar as reaction pressure. The MR was packed with a commercial Ru-based catalyst and a constant sweep gas flow rate in counter current mode was used. The influence of the temperature and the feed molar ratio on different parameters such as the ethanol conversion, the hydrogen production, the hydrogen yield and the CO-free hydrogen recovery has been evaluated.
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