کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
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61734 | 47601 | 2011 | 9 صفحه PDF | دانلود رایگان |
The influence of Rh concentration (0.005–0.15 wt.%) in NiOx(3 wt.%)/Al2O3 on the mechanism and kinetics of partial oxidation of methane (POM) to syngas was elucidated by combining steady-state catalytic tests over 120 h on stream with catalysts characterization and temporal analysis of products. All bi-metallic catalysts showed POM performance close to the thermodynamic one. The reaction mechanism does not depend on the nature of metals but is influenced by their reduction state. From a kinetic point of view, rhodium species (both reduced and oxidized) possess significantly higher activity toward methane conversion than the nickel ones. Rhodium fulfills a double role in the bi-metallic catalysts. Irrespective of its concentration, it promotes the reduction of Ni2+ in inactive NiAlxOy to metallic Ni directly under POM conditions. This is a reason for the higher activity and selectivity of low Rh-loaded (0.005 wt.%) NiOx(3 wt.%)/Al2O3 catalyst compared to its respective mono-metallic counterparts. Owing to the high activity of rhodium species, they alone determine the POM performance of higher Rh-loaded catalysts.
Mechanistic scheme of the synergetic effect of Rh on NiOx(3 wt.%)/Al2O3 in the POM reaction.Figure optionsDownload high-quality image (128 K)Download as PowerPoint slideHighlights
► NiOx/Al2O3 promoted with Rh traces for partial oxidation of methane (POM) to syngas.
► Reductive activation of the catalysts is not required for producing syngas.
► Rh traces help to reduce inactive NiAlxOy to active Ni0 in situ during POM reaction.
► The promotion with Rh does not change the reaction mechanism.
► Rh strongly increases the activation of methane.
Journal: Journal of Catalysis - Volume 280, Issue 1, 16 May 2011, Pages 116–124