中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
Syngas production using an oxygen-permeating membrane reactor with cofeed of methane and carbon dioxide

文献类型:期刊论文

作者Shao, ZP; Dong, H; Xiong, GX; Yang, WS
刊名chinese chemical letters
出版日期2000-07-01
卷号11期号:7页码:631-634
关键词ceramic membrane reactor oxygen permeation methane syngas
英文摘要ch4-co2-o-2 reforming to syngas in a never ba0.5sr0.5co0.8fe0.2o3.delta oxygen-permeable membrane reactor using lilanio/gamma-al2o3 as catalyst was successfully reported. excellent reaction performance was achieved with around 92% methane conversion efficiency, 95% co2 conversion rate, and nearly 8.5ml/min.cm(2) oxygen permeation flux. in contrast to the oxygen permeation model with the presence of large concentration of co2 (under such condition the oxygen permeation flux deteriorates with time), the oxygen permeation flux is really stable under the ch4co2-o-2 reforming condition.
WOS标题词science & technology ; physical sciences
类目[WOS]chemistry, multidisciplinary
研究领域[WOS]chemistry
关键词[WOS]oxidation ; catalysts ; oxide
收录类别SCI
原文出处true
语种英语
WOS记录号WOS:000088176300023
公开日期2010-11-30
源URL[http://159.226.238.44/handle/321008/85155]  
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
Shao, ZP,Dong, H,Xiong, GX,et al. Syngas production using an oxygen-permeating membrane reactor with cofeed of methane and carbon dioxide[J]. chinese chemical letters,2000,11(7):631-634.
APA Shao, ZP,Dong, H,Xiong, GX,&Yang, WS.(2000).Syngas production using an oxygen-permeating membrane reactor with cofeed of methane and carbon dioxide.chinese chemical letters,11(7),631-634.
MLA Shao, ZP,et al."Syngas production using an oxygen-permeating membrane reactor with cofeed of methane and carbon dioxide".chinese chemical letters 11.7(2000):631-634.

入库方式: OAI收割

来源:大连化学物理研究所

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