Oxidative dehydrogenation of propane to propylene over VO x /CaO–γ-Al 2 O 3 using lattice oxygen
Oxidative dehydrogenation (ODH) of propane to propylene is studied using a new vanadium catalyst supported on CaO–γ-Al 2 O 3 under a gas phase oxygen free atmosphere. The catalysts are synthesized with different CaO/γ-Al 2 O 3 ratios, keeping the vanadium loading at 10 percent. The prepared catalyst...
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Veröffentlicht in: | Catalysis science & technology 2016, Vol.6 (13), p.5154-5167 |
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Hauptverfasser: | , , , , , |
Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | Oxidative dehydrogenation (ODH) of propane to propylene is studied using a new vanadium catalyst supported on CaO–γ-Al
2
O
3
under a gas phase oxygen free atmosphere. The catalysts are synthesized with different CaO/γ-Al
2
O
3
ratios, keeping the vanadium loading at 10 percent. The prepared catalysts are characterized using various physicochemical techniques. Raman spectroscopy reveals that the catalysts have monovanadate and polyvanadate surface species (VO
x
) with minute crystal particles of V
2
O
5
. FTIR spectroscopy and XRD analysis confirm the presence of V
2
O
5
, CaO and γ-Al
2
O
3
in the catalyst. The catalysts show stable reduction and re-oxidation behavior in repeated TPR and TPO cycles, respectively. NH
3
-TPD shows that catalyst acidity decreases with increasing CaO content. The NH
3
-TPD kinetics analysis reveals that the activation energy of desorption increases with higher CaO, indicating stronger active site–support interactions. The ODH of propane experiments are conducted in a fluidized CREC Riser Simulator under gas phase oxygen free conditions. Among the studied catalysts, VO
x
/CaO–γ-Al
2
O
3
(1 : 1) displays the highest propane conversion (65%) and propylene selectivity (85%) and a low CO
x
due to its excellent oxygen carrying capacity, balanced acidity and moderate active site–support interactions. |
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ISSN: | 2044-4753 2044-4761 |
DOI: | 10.1039/C6CY00078A |