Methane steam reforming and ethanol steam reforming using a Ni(II)-Al(III) catalyst prepared from lamellar double hydroxides

被引:32
|
作者
Comas, J [1 ]
Dieuzeide, ML [1 ]
Baronetti, G [1 ]
Laborde, M [1 ]
Amadeo, N [1 ]
机构
[1] Ciudad Sanitaria & Univ Vall Hebron, Fac Ingn, Dpto Ingn Quim, Lab Proc Cataliticos, RA-1428 Buenos Aires, DF, Argentina
关键词
steam reforming; methane; ethanol; hydrogen production; Ni(II)-Al(III) LDH;
D O I
10.1016/j.cej.2006.01.003
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this work the methane steam reforming (MSR) and the ethanol steam reforming (ESR) on Ni(II)-Al(III) catalyst prepared from lamellar double hydroxides (LDHs) as precursor are studied. A comprehensive analysis of the kinetics results obtained at different water/methane and water/ethanol feed ratio and its correlation with the structural characteristic and redox behavior of the catalyst is carried out. The results show evidence that the catalyst behavior is related with the presence of only one type of active site in the Ni/Al2O3 catalyst. The competition for the active sites between reactants is verified for MSR. This behavior is also observed in ethanol steam reforming since methane steam reforming determines the products distribution in the exit stream. There would be an optimum inlet water concentration that gives a maximum performance in terms of H, and CO, selectivity and, simultaneously, a minimum CO selectivity. This is a promissory result taking into account that the hydrogen flow entering a PEM fuel-cell requires a CO concentration lower than 20 ppm. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:11 / 15
页数:5
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