作者: M.A. El-Bousiffi , D.J. Gunn
DOI: 10.1016/J.IJHEATMASSTRANSFER.2006.07.006
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摘要: Abstract A microreactor has been operated over cycles of temperature, feed composition, and pressure for the steam-reforming methane a nickel-based catalyst. The temperature range was 600 °C to 840 °C 1-10 bar. influence cyclical changes upon reactor gas exit compositions usually reversible, but introduction experiments at 800 °C increased catalyst activity subsequent operation 700 °C many hours operation.