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• W2023365430 abstract "This paper studies the effect of adding a CO-shift reactor downstream from a fluidized-bed biomass gasifier and a steam-reforming catalytic bed. The upstream gasifier was of small pilot-plant scale, 10 (kg of biomass)/h, so the downstream catalytic reactors, steam-reformer and CO-shift, operated under a real gasification gas. The main gasifying agent used was H2O−O2 mixtures. Some results are also reported for gasification with air with some steam. The CO-shift catalytic system used had one high- (HT) and one low-temperature (LT) reactor. Commercial catalysts were used. CO conversions (eliminations) higher than 90% and a H2 content as high as 73 vol %, dry basis, have been obtained by the CO-shift system. The CO conversion and the increase (up to 14 vol %) of H2 content correlated well with the molar steam/CO ratio in the gasification gas at the inlet of the HT reactor." @default.
• W2023365430 created "2016-06-24" @default.
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• W2023365430 date "2006-03-16" @default.
• W2023365430 modified "2023-10-18" @default.
• W2023365430 title "Hydrogen Production by Biomass Gasification with Steam−O₂ Mixtures Followed by a Catalytic Steam Reformer and a CO-Shift System" @default.
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• W2023365430 doi "https://doi.org/10.1021/ef050428p" @default.
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