Abstract
The oxidative dehydrogenation of n-butane under anaerobic conditions was studied using three catalysts prepared based on a mixture of vanadium with magnesium oxides, one without a support (B16) and two supported over a 30 wt % of a third oxide, SiO2 (S16) or α-Al2O3 (A16). The n-butane conversion and the selectivity toward butadiene decreased as the time on run increased. The reaction rate control gradually changed from chemical to the diffusion of oxygen through the catalyst structure as the time on run increased, with a selectivity always higher than in aerobic conditions. Supported catalysts were more active than the non-supported one. After reoxidation, the catalysts recovered the original activity and selectivity without any damage to the visible structure. During the reduction cycle, a decrease in the amount of V5+ with the simultaneous appearance of increasing amounts of V4+. The presence of a lower oxidation state was never found and after reoxidation, the only species present was V5+. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montréal, Quebec, Canada 8/23-27/2009).
| Original language | English |
|---|---|
| Pages | nopagegiven |
| State | Published - 2009 |
| Externally published | Yes |
| Event | 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering - Montreal, QC, Canada Duration: 23 Aug 2009 → 27 Aug 2009 |
Conference
| Conference | 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering |
|---|---|
| Country/Territory | Canada |
| City | Montreal, QC |
| Period | 23/08/09 → 27/08/09 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
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