中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
Aqueous-phase catalytic process for production of pentane from furfural over nickel-based catalysts

文献类型:期刊论文

作者Zhang Xinghua1,2; Wang Tiejun1; Ma Longlong1; Wu Chuangzhi1
刊名fuel
出版日期2010-10-01
卷号89期号:10页码:2697-2702
关键词Biomass Furfural Ni Bifunctional catalyst Pentane
ISSN号0016-2361
产权排序[zhang xinghua; wang tiejun; ma longlong; wu chuangzhi] chinese acad sci, guangzhou inst energy convers, key lab renewable energy & gas hydrate, guangzhou 510640, guangdong, peoples r china; [zhang xinghua] chinese acad sci, grad sch, beijing 100049, peoples r china
通讯作者wangtj@ms.giec.ac.cn
中文摘要supported nickel catalysts for aqueous-phase catalytic hydrogenation/dehydration of furfural were prepared using impregnation method with different supporting materials. effects of supporting materials, nickel loading and reaction temperature on conversion rate of furfural as well as selectivity for desired product c(5) were systematically studied. experiments showed that catalytic activity of ni/sio(2)-al(2)o(3) was obviously higher than that of ni/gamma-al(2)o(3). the conversion of furfural over 14 wt.%ni/sio(2)-al(2)o(3) catalyst was 62.99% under the temperature of 140 degrees c and the cold pressure of h(2) 3.0 mpa, while that was 19.19% over 14 wt.%ni/gamma-al(2)o(3) under the same conditions. conversion rate of furfural increased with temperature, but selectivity for desired product decreased with temperature. tentative reaction mechanisms of hydrogenation/dehydration were proposed. in order to investigate catalyst recyclability, a batch of ni/sio(2)-al(2)o(3) was reused three times and analyzed by thermogravimetry (tg). it was found that considerable amount of coke formed on ni/sio(2)-al(2)o(3) surface and deteriorated its activity dramatically after second use.
英文摘要supported nickel catalysts for aqueous-phase catalytic hydrogenation/dehydration of furfural were prepared using impregnation method with different supporting materials. effects of supporting materials, nickel loading and reaction temperature on conversion rate of furfural as well as selectivity for desired product c(5) were systematically studied. experiments showed that catalytic activity of ni/sio(2)-al(2)o(3) was obviously higher than that of ni/gamma-al(2)o(3). the conversion of furfural over 14 wt.%ni/sio(2)-al(2)o(3) catalyst was 62.99% under the temperature of 140 degrees c and the cold pressure of h(2) 3.0 mpa, while that was 19.19% over 14 wt.%ni/gamma-al(2)o(3) under the same conditions. conversion rate of furfural increased with temperature, but selectivity for desired product decreased with temperature. tentative reaction mechanisms of hydrogenation/dehydration were proposed. in order to investigate catalyst recyclability, a batch of ni/sio(2)-al(2)o(3) was reused three times and analyzed by thermogravimetry (tg). it was found that considerable amount of coke formed on ni/sio(2)-al(2)o(3) surface and deteriorated its activity dramatically after second use. (c) 2010 elsevier ltd. all rights reserved.
WOS标题词science & technology ; technology
学科主题energy & fuels ; engineering
类目[WOS]energy & fuels ; engineering, chemical
研究领域[WOS]energy & fuels ; engineering
关键词[WOS]supported metal-catalysts ; aldol-condensation ; oxygenated hydrocarbons ; bio-oil ; biomass ; hydrogenation ; alkanes ; dehydration ; chemicals ; silica
收录类别SCI
资助信息national natural science foundation of china [50776092]; chinese academy of science [kscx2-yw-g-063]
原文出处https://dx.doi.org/10.1016/j.fuel.2010.05.043
语种英语
WOS记录号WOS:000279737500004
公开日期2014-12-24
源URL[http://ir.giec.ac.cn/handle/344007/8483]  
专题中国科学院广州能源研究所
生物质能研究中心
生物质化工品制备实验室
作者单位1.Chinese Acad Sci, Guangzhou Inst Energy Convers, Key Lab Renewable Energy & Gas Hydrate, Guangzhou 510640, Guangdong, Peoples R China
2.Chinese Acad Sci, Grad Sch, Beijing 100049, Peoples R China
推荐引用方式
GB/T 7714
Zhang Xinghua,Wang Tiejun,Ma Longlong,et al. Aqueous-phase catalytic process for production of pentane from furfural over nickel-based catalysts[J]. fuel,2010,89(10):2697-2702.
APA Zhang Xinghua,Wang Tiejun,Ma Longlong,&Wu Chuangzhi.(2010).Aqueous-phase catalytic process for production of pentane from furfural over nickel-based catalysts.fuel,89(10),2697-2702.
MLA Zhang Xinghua,et al."Aqueous-phase catalytic process for production of pentane from furfural over nickel-based catalysts".fuel 89.10(2010):2697-2702.

入库方式: OAI收割

来源:广州能源研究所

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