中国科学院机构知识库网格
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Hydrogen production from the steam reforming of liquid hydrocarbons in membrane reactor

文献类型:期刊论文

作者Chen, Yazhong; Xu, Hengyong; Wang, Yuzhong; Xiong, Guoxing
刊名catalysis today
出版日期2006-10-30
卷号118期号:1-2页码:136-143
关键词hydrogen production liquid hydrocarbons steam reforming palladium membrane reactor nickel catalyst
产权排序1;1
通讯作者熊国兴
英文摘要hydrogen production from the steam reforming of liquid hydrocarbons over a self-made nickel catalyst was investigated in a fixed bed palladium membrane reactor (pmr). the reactions were carried out at 723-823 k and 200-900 kpa. the applied pd membrane was developed by a novel electroless plating method. the influences of working conditions on the performance of the pmr were also studied. the results indicate that the membrane has a h-2 permeance of 50.0 m(3) m(-2) h(-1) bar(-1) and a h-2/n-2 separation coefficient of 1200, determined at 773 k and transmembrane pressure of 100 kpa using a single gas method. owing to the selective removal of h2 by the membrane, the yield of h-2 greatly increased; meanwhile the yield of ch4 efficiently decreased. the purity of h2 in the permeate side of membrane could be maintained over 99.5%. h2 production capacity of the pmr could be as high as 23.1 m(3) m(-2) h(-1) (m(3) h-2 per m(2) membrane area per hour) under optimized working conditions. the reactions in the steam reforming of liquid hydrocarbons and h2 separation are highly integrated in the pmr, which suggests that the steam reforming of liquid hydrocarbons in pmr could be an attractive process for h-2 production under mild reaction conditions. (c) 2006 elsevier b.v. all rights reserved.
WOS标题词science & technology ; physical sciences ; technology
类目[WOS]chemistry, applied ; chemistry, physical ; engineering, chemical
研究领域[WOS]chemistry ; engineering
关键词[WOS]palladium membrane ; fuel-cells ; methane ; dehydrogenation ; optimization ; behavior ; heptane
收录类别ISTP ; SCI
原文出处true
语种英语
WOS记录号WOS:000241489700020
公开日期2010-11-30
源URL[http://159.226.238.44/handle/321008/97647]  
专题大连化学物理研究所_中国科学院大连化学物理研究所
作者单位1.Chinese Acad Sci, Dalian Inst Chem Phys, Nat Gas Utilizat & Appl Catalysis Lab, Dalian 116023, Peoples R China
2.Chinese Acad Sci, Dalian Inst Chem Phys, State Key Lab Catalysis, Dalian 116023, Peoples R China
推荐引用方式
GB/T 7714
Chen, Yazhong,Xu, Hengyong,Wang, Yuzhong,et al. Hydrogen production from the steam reforming of liquid hydrocarbons in membrane reactor[J]. catalysis today,2006,118(1-2):136-143.
APA Chen, Yazhong,Xu, Hengyong,Wang, Yuzhong,&Xiong, Guoxing.(2006).Hydrogen production from the steam reforming of liquid hydrocarbons in membrane reactor.catalysis today,118(1-2),136-143.
MLA Chen, Yazhong,et al."Hydrogen production from the steam reforming of liquid hydrocarbons in membrane reactor".catalysis today 118.1-2(2006):136-143.

入库方式: OAI收割

来源:大连化学物理研究所

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