Abstract
The oxidative dehydrogenation of propane was investigated in a fixed-bed tubular flow reactor at 350 and 450°C over V–Mg–O catalysts prepared via a solid reaction (the mix-VMg catalysts) or from mesoporous precursors (the meso-VMg catalysts). Significantly higher selectivities and yields to propene were obtained over the meso-VMg catalysts than over the mix-VMg ones. The cooperation between a much higher BET specific surface area and a novel phase, a highly dispersed-Mg-in-V2O3, is suggested as responsible for the higher ODP performance of the meso-VMg catalysts than of the mix-VMg ones.
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Chao, ZS., Ruckenstein, E. V–Mg–O Prepared via a Mesoporous Pathway: A Low-Temperature Catalyst for the Oxidative Dehydrogenation of Propane to Propene. Catalysis Letters 94, 217–221 (2004). https://doi.org/10.1023/B:CATL.0000020576.75053.96
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DOI: https://doi.org/10.1023/B:CATL.0000020576.75053.96