The nature of support and type of active metal affect catalytic performance. In this work
the effect of using La
2
O
3
as promoter and support for Ni/γ-Al
2
O
3
catalysts in dry reforming of methane was investigated. The reforming reactions were carried out at atmospheric pressure in the temperature range of 500-700℃. The activity and stability of the catalyst
carbon formation
and syngas (H
2
/CO) ratio were determined. Various techniques were applied for characterization of both fresh and used catalysts. Addition of La
2
O
3
to the catalyst matrix improved the dispersion of Ni and adsorption of CO
2
thus its activity and stability enhanced.
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