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题名: Catalytic partial oxidation of methane to synthesis gas over Ni/gamma-Al2O3 catalyst in a fluidized-bed
作者: Ji, YY;  Li, WZ;  Xu, HY;  Chen, YX
关键词: catalytic partial oxidation ;  methane to syngas ;  fluidized-bed reactor
刊名: APPLIED CATALYSIS A-GENERAL
发表日期: 2001-05-14
卷: 213, 期:1, 页:25-31
收录类别: SCI
文章类型: Article
WOS标题词: Science & Technology ;  Physical Sciences ;  Life Sciences & Biomedicine
类目[WOS]: Chemistry, Physical ;  Environmental Sciences
研究领域[WOS]: Chemistry ;  Environmental Sciences & Ecology
英文摘要: The catalytic partial oxidation of methane to synthesis gas over Ni/gamma -Al2O3 catalyst has been investigated in a fluidized-bed reactor. The results showed that an isothermal operation and the performance near to thermodynamic equilibrium could be obtained in a fluidized-bed reactor. A study on carbon deposit showed that there was a low rate of carbon formation in a fluidized-bed reactor. The CH4 conversion as well as CO and H-2 selectivities remained constant at similar to 92, similar to 94 and similar to 99.0%, respectively, during 100h running. Neither phase transformation of the support nor remarkable Ni loss was found on the catalyst after 100h running. (C) 2001 Elsevier Science B.V. All rights reserved.
关键词[WOS]: CARBON-MONOXIDE ;  CONVERSION ;  HYDROGEN ;  CO
语种: 英语
WOS记录号: WOS:000168458400002
Citation statistics: 
内容类型: 期刊论文
URI标识: http://cas-ir.dicp.ac.cn/handle/321008/139039
Appears in Collections:中国科学院大连化学物理研究所_期刊论文

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作者单位: 1.Chinese Acad Sci, Dalian Inst Chem Phys, Dalian 116023, Peoples R China

Recommended Citation:
Ji, YY,Li, WZ,Xu, HY,et al. Catalytic partial oxidation of methane to synthesis gas over Ni/gamma-Al2O3 catalyst in a fluidized-bed[J]. APPLIED CATALYSIS A-GENERAL,2001,213(1):25-31.
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