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To develop small stationary reformers for on-site H2 production, the active catalyst and its reaction kinetics were examined in order to study the steam methane reforming reaction. A 20 wt% Ni/γ-Al2O3 was found to be a highly active catalyst within the investigated range of contact time from 1.16 to 3.64 gcath/mol, which was good for developing the small stationary reformers. BET, XRD, and TEM analysis...
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