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
Hauptverfasser: Ayandiran, Afees A., Bakare, Idris A., Binous, Housam, Al-Ghamdi, Sameer, Razzak, Shaikh A., Hossain, Mohammad M.
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.
ISSN:2044-4753
2044-4761
DOI:10.1039/C6CY00078A