Methane conversion reactions on Ni catalysts promoted with Rh: Influence of support

被引:70
作者
Lucredio, Alessandra F. [1 ]
Assaf, Jose M. [2 ]
Assaf, Elisabete M. [1 ]
机构
[1] Univ Sao Paulo, Inst Quim Sao Carlos, BR-13560970 Sao Carlos, SP, Brazil
[2] Univ Fed Sao Carlos, BR-13565905 Sao Carlos, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
Catalyst; Nickel; Hydrotalcite; Methane; Reforming; SOLID-SOLUTION CATALYSTS; PARTIAL OXIDATION; HYDROGEN-PRODUCTION; DIMETHYL ETHER; NOBLE-METALS; CO2; TEMPERATURE; ACTIVATION; LANTHANUM; SYSTEMS;
D O I
10.1016/j.apcata.2011.04.035
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
Ni catalysts supported on gamma-Al(2)O(3) and Mg(Al)O were prepared with and without Rh as a promoter and tested in the reforming of methane in the presence of excess methane, simulating a model biogas. The effects of adding synthetic air on the methane conversion and the formation of carbon were assessed. The catalysts were characterized by X-ray spectroscopy (EDS), surface area (BET), X-ray diffraction (XRD), Temperature-programmed reduction (TPR), X-ray absorption near-edge structure (XANES) and XPD. The results showed that in catalysts without Rh, the Ni interacts strongly with the supports, showing high reduction temperatures in TPR tests. The addition of Rh increased the amount of reducible Ni and facilitated the reduction of the species interacting strongly with the support. In the catalytic tests, the samples promoted with Rh suffered higher carbon deposition. The in situ XPD suggested that on the support gamma-Al(2)O(3), the presence of Rh probably led to a segregation of Ni species with time on stream, leading to carbon deposition. On the support MgAlO, the presence of Rh improved the dispersion of Ni, by reducing the Ni(0) crystallite size, suggesting that in this case the carbon deposition was due to a favoring of CH(4) decomposition by Rh. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:156 / 165
页数:10
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