4.8 Article

Steam reforming of ethanol by non-noble metal catalysts

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PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.rser.2023.113184

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Hydrogen; Ethanol steam reforming; Catalysis; Product yields; Kinetics; Modeling; Scale-up; Solar reactor

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Catalytic steam reforming of ethanol (CSRE) is a promising method for hydrogen production. Ethanol can be derived from low-cost carbohydrates or biomass through fermentation. This study explores the use of novel non-noble catalysts, impregnated in alpha-Al2O3, for CSRE. The catalytic experiments demonstrate high hydrogen yields and negligible catalyst deactivation. Pilot-scale investigations have been initiated.
Catalytic steam reforming of ethanol (CSRE) is an attractive mode of producing hydrogen as an environmentally -friendly energy carrier. Ethanol can be produced from first-generation fermenting of cheap carbohydrates (e.g. non-food cassava and agricultural residues), and second-generation fermenting of biomass. The catalytic con-version of ethanol requires an appropriate catalyst, operating temperature, and reaction time. Supported noble metal catalysts were previously used. The present work uses novel non-noble catalysts. The most efficient cat-alysts were impregnated in alpha-Al2O3 and fully characterized. The catalytic experiments were conducted between 500 degrees C and 600 degrees C in either electrically-heated fixed bed reactors, or in a solar-heated fluidized bed reactor. The main reaction products were H2 (approximately 5.5 mol H2/mol ethanol), CO, CO2 and CH4. Deactivation of the Co/alpha-Al2O3 catalyst was not observed. Negligible amounts of acetone and acetaldehyde were detected. A maximum hydrogen yield of over 95% was achieved. Pilot-scale investigations were started.

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