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Characterization and activity in dry reforming of methane on NiMg/Al and Ni/MgO catalysts

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Characterization and activity in dry reforming of methane on NiMg/Al

and Ni/MgO catalysts

Authors

Abdelhamid Djaidja, S Libs, A Kiennemann, A Barama

Publication date 2006/4/15 Journal Catalysis Today Volume 113 Issue 3-4 Pages 194-200 Publisher Elsevier Description

Dry reforming of methane has been investigated on two series of catalysts either prepared by co-precipitation: n(NixMgy)/Al, NixMgy and NixAly or prepared by impregnation: Ni/MgO (mol% Ni = 5, 10).

The catalysts, calcined at 600–900 °C, were characterized by different techniques: BET, H2-TPR,

TPO, XRD, IR, and TEM-EDX analysis. The surface BET (30–182 m2 g−1) decreased with increasing

the temperature of calcination, after reduction and in the presence of Mg element. The XRD analysis showed, for n(NixMgy)/Al catalysts, the presence of NiAl2O4 and NiO–MgO solid solutions. The catalyst

reducibility decreased with increasing the temperature of pretreatment. The n(NixMgy)/Al catalysts

were active for dry reforming of methane with a good resistance to coke formation. The bimetallic catalyst Ni0.05Mg0.95 (calcined at 750 °C and tested at 800 °C) presents a poor activity. In contrast, the

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