Abstract

Vanadia/silica particles with a specific surface area up to 330 m 2 g −1 and a V 2O 5 content up to 50 wt.% or V surface density up to 27.6 V nm −2 were prepared by flame spray pyrolysis. The catalysts were characterized by nitrogen adsorption, X-ray diffraction, temperature-programmed reduction, Raman spectroscopy, and 51V MAS NMR and tested in the oxidative dehydrogenation (ODH) of propane. Depending on vanadia content, different vanadia species were formed. The as-prepared flame-made catalysts showed dominantly isolated monomeric VO x surface species for V loadings exceeding even the typical “monolayer coverage” (2 V nm −2) of classic wet-impregnated materials. The stability of these VO x species depended on temperature and V surface density. Catalysts with 3.3 V nm −2 were stable up to 500 °C and those with 2 V nm −2 up to 600 °C. Catalysts loaded with 3–25 wt.% V 2O 5 were tested for the ODH of propane. Catalysts containing ⩾15 wt.% V 2O 5 showed structural rearrangement of the VO x species during the catalytic tests inducing a transition from monomeric to crystalline vanadia. The turnover frequency of flame-made catalysts decreased with increasing vanadia loading, indicating a higher activity of monomeric VO x species compared to crystalline V 2O 5. The conversion (global activity), however, showed a maximum for the 20 wt.% V 2O 5/SiO 2 (4.6 V nm −2) catalyst. The selectivity to propene depended mainly on propane conversion and only to a lesser extent on the structure of the VO x species. Highest selectivity (55%) was achieved for the low loaded catalysts. With increasing vanadia loading, formation of CO x increased and the product ratio of CO 2/CO decreased. Highest propene yield was measured for catalysts with relative high V surface density containing both monomeric VO x and crystalline V 2O 5. Flame spray pyrolysis proved to be a very versatile method for synthesis of V 2O 5/SiO 2 catalysts with high dispersion of isolated VO x species at high surface density.

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