Hydrogen production through alcohol steam reforming on Cu/ZnO-based catalysts

被引:69
|
作者
Lorenzut, Barbara [1 ,2 ]
Montini, Tiziano [1 ,2 ]
De Rogatis, Loredana [1 ,2 ]
Canton, Patrizia [3 ]
Benedetti, Alvise [3 ]
Fornasiero, Paolo [1 ,2 ]
机构
[1] Univ Trieste, ICCOM CNR Trieste Res Unit, Dept Chem, I-34127 Trieste, Italy
[2] Univ Trieste, INSTM, I-34127 Trieste, Italy
[3] Univ Ca Foscari Venezia, Dept Phys Chem, I-30170 Venice, Italy
关键词
Ethanol reforming; Hydrogen production; Cu/Zn/Al2O3 based catalysts; SUPPORTED COBALT CATALYSTS; FUEL-CELL; OXIDE CATALYSTS; ZNO CATALYSTS; CU CATALYSTS; METHANOL; ETHANOL; COPPER; NI; MECHANISM;
D O I
10.1016/j.apcatb.2010.10.009
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
Hydrogen production by steam reforming of methanol and ethanol is studied over a series of Cu/ZnO/Al2O3 catalysts prepared by different coprecipitation procedures and modified with the introduction of Ni and Co. The catalysts are characterized using N-2 physisorption, X-ray diffraction (XRD), temperature programmed reduction (TPR) techniques, N2O decomposition, high resolution transmission electron microscopy (HR-TEM) and thermogravimetric analysis (TGA). Despite the influence of the preparation method on the texture and structure of Cu/ZnO/Al2O3 catalysts, their catalytic behavior appears not significantly affected. While Cu/ZnO/Al2O3 shows poor H-2 selectivity in the ethanol steam reforming reaction, the presence of a second metal (Ni or Co) significantly improves the reforming reaction. Although coke deposition remains a drawback for these systems, formation of an alloy between Ni and Cu appreciably reduces carbon deposition with respect to the Co/Cu-based system. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:397 / 408
页数:12
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