Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
5147697 | International Journal of Hydrogen Energy | 2016 | 13 Pages |
Abstract
The reaction rate of low-temperature steam reforming was studied over two Ni-based catalysts. Experimental tests were carried out for temperatures between 400 and 550 °C and pressures between 1 and 7 bar, using methane and simulated biogas (1:1 methane-carbon dioxide mixture) as carbonaceous feed. The results were analyzed with a simplified reaction rate expression. The parameters of such expression were optimized in order to provide a tool for the design of an industrial scale reactor using the catalysts considered.
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Authors
L. Turchetti, M.A. Murmura, G. Monteleone, A. Giaconia, A.A. Lemonidou, S.D. Angeli, V. Palma, C. Ruocco, M.C. Annesini,