Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
7711857 | International Journal of Hydrogen Energy | 2016 | 8 Pages |
Abstract
Regularities of the processes of dry reforming of methane (DRM), ethanol (DRE) and modeling mixture of fermentation products (DRFP) to hydrogen and syngas over Ni-Co-containing porous ceramic membrane-catalytic converters(PCMCC), obtained by self-propagating high temperature synthesis (SHS), were studied. The non-additive effect of increasing the catalytic activity in the processes over Ni-Co3O4 (50-50%) PCMCC was discovered. It was shown that in the PCMCC the processes more intensified in comparison to the implementation of the processes in a flow reactor with a fixed bed of granular catalyst of the same composition.
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Authors
Mark V. Tsodikov, Alexey S. Fedotov, Dmitriy O. Antonov, Valeriy I. Uvarov, Victor Yu Bychkov, Francis C. Luck,