Abstract
The carbon dioxide reforming of methane over Ni/SiO2, Ni–Co/SiO2 and commercial nickel catalyst was investigated. The best methane conversion (57%) and H2 (53%) yield were achieved over Ni industrial catalyst. This catalyst, however, undergoes deactivation as a result of carbon formation. The advantage of the bimetallic catalysts is high resistance to metal reduction and coking.
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Michalkiewicz, B., Sreńscek-Nazzal, J. & Ziebro, J. Optimization of Synthesis Gas Formation in Methane Reforming with Carbon Dioxide. Catal Lett 129, 142–148 (2009). https://doi.org/10.1007/s10562-008-9797-6
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DOI: https://doi.org/10.1007/s10562-008-9797-6