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
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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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