Steam reforming of ethanol by non-noble metal catalysts

被引:27
|
作者
Deng, Yimin [1 ]
Li, Shuo [2 ]
Appels, Lise [1 ]
Zhang, Huili [3 ]
Sweygers, Nick [1 ]
Baeyens, Jan [1 ,2 ]
Dewil, Raf [1 ]
机构
[1] Katholieke Univ Leuven, Dept Chem Engn, Proc & Environm Technol Lab, B-2860 St Katelijne Waver, Belgium
[2] Beijing Univ Chem Technol, Beijing Adv Innovat Ctr Soft Matter Sci & Engn, Beijing 100029, Peoples R China
[3] Beijing Univ Chem Technol, Coll Life Sci & Technol, Beijing 100029, Peoples R China
来源
关键词
Hydrogen; Ethanol steam reforming; Catalysis; Product yields; Kinetics; Modeling; Scale-up; Solar reactor; NI-BASED CATALYSTS; CO-BASED CATALYSTS; HYDROGEN-PRODUCTION; IN-SITU; BIO-ETHANOL; AP-XPS; COBALT; PERFORMANCE; CERIA; DESIGN;
D O I
10.1016/j.rser.2023.113184
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
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.
引用
收藏
页数:17
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