Hydrogen production from catalytic steam reforming of bio-oil aqueous fraction over Ni/CeO2-ZrO2 catalysts | |
Yan, Chang-Feng1,2; Cheng, Fei-Fei1,2; Hu, Rong-Rong1 | |
刊名 | international journal of hydrogen energy |
2010-11-01 | |
卷号 | 35期号:21页码:11693-11699 |
关键词 | Ni/CeO2-ZrO2 Hydrogen Bio-oil Steam reforming |
ISSN号 | 0360-3199 |
通讯作者 | yancf@ms.giec.ac.cn |
产权排序 | [yan, chang-feng; cheng, fei-fei; hu, rong-rong] chinese acad sci, guangzhou inst energy convers, guangzhou 510640, peoples r china; [yan, chang-feng; cheng, fei-fei] chinese acad sci, grad univ, beijing 100049, peoples r china |
中文摘要 | a series of composite catalysts ni/ceo2-zro2 were prepared via impregnation method with ni as the active metal. a laboratory-scale fixed-bed reactor was employed to investigate the catalyst performance during hydrogen production by steam reforming bio-oil aqueous fraction. effects of water-to-bio-oil ratio (w/b), reaction temperature, and the loaded weight of ni and ce on the hydrogen production performance of nil ceo2-zro2 catalysts were examined. the obtained results were compared with commercial nickel-based catalysts (z417). the best performance of ni/ceo2-zro2 catalyst was observed when the ni and ce loaded weight were 12% and 7.5% respectively. at w/b = 4.9, t = 800 degrees c, h-2 yield reaches the highest of 69.7% and h-2 content of 61.8% were obtained. under the same condition, h-2 yield and h-2 content were higher than commercial nickel-based catalysts (z417). (c) 2010 professor t. nejat veziroglu. published by elsevier ltd. all rights reserved. |
英文摘要 | a series of composite catalysts ni/ceo2-zro2 were prepared via impregnation method with ni as the active metal. a laboratory-scale fixed-bed reactor was employed to investigate the catalyst performance during hydrogen production by steam reforming bio-oil aqueous fraction. effects of water-to-bio-oil ratio (w/b), reaction temperature, and the loaded weight of ni and ce on the hydrogen production performance of nil ceo2-zro2 catalysts were examined. the obtained results were compared with commercial nickel-based catalysts (z417). the best performance of ni/ceo2-zro2 catalyst was observed when the ni and ce loaded weight were 12% and 7.5% respectively. at w/b = 4.9, t = 800 degrees c, h-2 yield reaches the highest of 69.7% and h-2 content of 61.8% were obtained. under the same condition, h-2 yield and h-2 content were higher than commercial nickel-based catalysts (z417). (c) 2010 professor t. nejat veziroglu. published by elsevier ltd. all rights reserved. |
学科主题 | chemistry ; electrochemistry ; energy & fuels |
WOS标题词 | science & technology ; physical sciences ; technology |
类目[WOS] | chemistry, physical ; electrochemistry ; energy & fuels |
研究领域[WOS] | chemistry ; electrochemistry ; energy & fuels |
关键词[WOS] | acetic-acid ; fast-pyrolysis ; biomass pyrolysis ; nickel-catalysts ; metal-catalysts ; model compounds ; bed reactor ; temperature ; ethanol ; gasification |
收录类别 | SCI |
资助信息 | natural science foundation of china [20806082, 50306026] |
原文出处 | https://dx.doi.org/10.1016/j.ijhydene.2010.08.083 |
语种 | 英语 |
WOS记录号 | WOS:000283959900004 |
公开日期 | 2014-12-24 |
内容类型 | 期刊论文 |
源URL | [http://ir.giec.ac.cn/handle/344007/8479] |
专题 | 中国科学院广州能源研究所 |
作者单位 | 1.Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Peoples R China 2.Chinese Acad Sci, Grad Univ, Beijing 100049, Peoples R China |
推荐引用方式 GB/T 7714 | Yan, Chang-Feng,Cheng, Fei-Fei,Hu, Rong-Rong. Hydrogen production from catalytic steam reforming of bio-oil aqueous fraction over Ni/CeO2-ZrO2 catalysts[J]. international journal of hydrogen energy,2010,35(21):11693-11699. |
APA | Yan, Chang-Feng,Cheng, Fei-Fei,&Hu, Rong-Rong.(2010).Hydrogen production from catalytic steam reforming of bio-oil aqueous fraction over Ni/CeO2-ZrO2 catalysts.international journal of hydrogen energy,35(21),11693-11699. |
MLA | Yan, Chang-Feng,et al."Hydrogen production from catalytic steam reforming of bio-oil aqueous fraction over Ni/CeO2-ZrO2 catalysts".international journal of hydrogen energy 35.21(2010):11693-11699. |
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