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• W2017572521 startingPage "147" @default.
• W2017572521 abstract "Low temperature steam reforming of methane mainly to hydrogen and carbon dioxide (CH4 + 2H2O → 4H2 + CO2) has been performed at 773 and 823 K over a commercial nickel catalyst in an equilibrium-shift reactor with an 11-μm thick palladium membrane (Mem-L) on a stainless steel porous metal filter. The methane conversion with the reactor is significantly higher than its equilibrium value without membrane due to the equilibrium-shift combined with separation of pure hydrogen through the membrane. The methane conversion in a reactor with an 8-μm membrane (Mem-H) is similar to that with Mem-L, although the hydrogen permeance through Mem-H is almost double of that through Mem-L. The amount of hydrogen separated in the reaction with Mem-H is significantly large, showing that the hydrogen separation overwhelms the hydrogen production because of the insufficient catalytic activity." @default.
• W2017572521 created "2016-06-24" @default.
• W2017572521 creator A5001994620 @default.
• W2017572521 creator A5081923990 @default.
• W2017572521 date "2006-02-01" @default.
• W2017572521 modified "2023-10-08" @default.
• W2017572521 title "Pure hydrogen production by methane steam reforming with hydrogen-permeable membrane reactor" @default.
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• W2017572521 doi "https://doi.org/10.1016/j.cattod.2005.11.001" @default.
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