Production of hydrogen for MC fuel cell by steam reforming of ethanol over MgO supported Ni and Co catalysts

被引:193
作者
Freni, S
Cavallaro, S
Mondello, N
Spadaro, L
Frusteri, F
机构
[1] Univ Messina, Dipartimento Chim Ind & Ingn Mat, I-98166 Sant Agata Di Messina, Italy
[2] Ist CNR TAE, I-98126 Messina, Italy
关键词
Ni and Co catalysts; MgO carrier; H-2; production; ethanol steam reforming; fuel cell;
D O I
10.1016/S1566-7367(03)00051-7
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
. Steam reforming of ethanol, in simulated MCFC operative conditions was investigated over MgO supported Ni and Co catalysts. Ni/MgO catalysts exhibit higher activity and selectivity to H-2 than Co/MgO catalysts because of the lower tendency of Ni to oxidize during reaction and to promote carbon monoxide methanation and ethanol decomposition reactions. Coke formation was strongly depressed due to the benefits gained through the use of basic carrier (MgO). Endurance tests carried out at low gas hourly space velocity (10,000 h(-1)) for 630 h showed that Ni/MgO catalyst possesses adequate characteristics to be proposed as an efficient catalytic system for the production of hydrogen for MCFC. (C) 2003 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:259 / 268
页数:10
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