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Preferential oxidation of CO in H2-rich gases over Co-promoted Pt-γ-Al2O3 catalyst  ( SCI-EXPANDED收录 EI收录)  

文献类型:期刊文献

英文题名:Preferential oxidation of CO in H2-rich gases over Co-promoted Pt-γ-Al2O3 catalyst

作者:Yan, Jing[1]; Ma, Jianxin[2]; Cao, Ping[1]; Li, Ping[3]

机构:[1]Tongji Univ, Clean Energy Automot Engn Ctr, Shanghai 200092, Peoples R China;[2]E China Univ Sci & Technol, Inst Ind Catalysis, Shanghai 200237, Peoples R China;[3]E China Univ Sci & Technol, Ctr Chem React Engn, Shanghai 200237, Peoples R China

年份:2004

卷号:93

期号:1-2

起止页码:55

外文期刊名:CATALYSIS LETTERS

收录:;EI(收录号:2004188137598);WOS:【SCI-EXPANDED(收录号:WOS:000189103200011)】;

语种:英文

外文关键词:preferential oxidation of CO; hydrogen; Pt catalyst; promoter; cobalt; PEMFC

摘要:Carbon monoxide is a poison to the Pt anode in proton exchange membrane fuel cell (PEMFC). Preferential oxidation (PROX) is an effective method to reduce CO in hydrogen-rich gas streams to a tolerant level. In the present work, the effect of adding cobalt to Pt/gamma-Al2O3 on the PROX of CO was investigated. Our results showed that the addition of Co to Pt/gamma-Al2O3 could not only improve the low-temperature activity but also reduce significantly the loading of Pt in the catalysts. Over the catalyst 3% Co/1%Pt/ gamma-Al2O3 the conversion of CO was close to 100% at 90 degreesC and space velocity of 8000 mL g(-1) h(-1). In addition, the Co-promoted Pt/ gamma-Al2O3 catalyst showed good resistance to H2O and CO2 and could be operated in a wide range of space velocity. At temperatures above 90 degreesC, the existence of H2O in the feed increased the conversion and broadened the operating temperature range without worsening the selectivity. When space velocity was changed from 8000 to 80,000 mL g(-1) h(-1) and temperatures was kept between 120 and 160 degreesC, the conversion of CO was always over 99% and the decrease in O-2 selectivity did not exceed 10%. Furthermore, a strong opposite effect of the ratio of O-2 to CO on the conversion of CO and the selectivity of O-2 was observed. However, at the O-2/ CO ratio of 1.0 and temperatures between 120 and 160 degreesC, a satisfied balance between conversion and selectivity could be obtained.

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