Abstract

Vanadia was found to be well dispersed and present as a two-dimensional overlayer when supported on SiO2, TiO2, SnO2, 3 wt% TiO2/SiO2, 3 wt% MoO3/SiO2, and 3 wt% SnO2/SiO2. Partial oxidation of methane by oxygen formed formaldehyde most selectively over the V2O5/SiO2catalyst, but catalytic performance was strongly dependent on vanadia coverage and autocatalytic behavior was observed. At very low conversions, the formaldehyde activity increased linearly with vanadia coverage, indicating that isolated V5+species were responsible for the active sites. No significant structural changes were revealed byin situRaman spectroscopy for the V2O5/SiO2catalyst, which indicated that the fully oxidized surface sites were related to the high formaldehyde selectivity. This selectivity exhibited a maximum at 1 wt% V2O5content, and the lower selectivities at higher loadings appeared to be due to the increasing Lewis acidity of the catalysts. Space–time yields of 0.1–1.4 kg CH2O/kg cat/hr and selectivities of 2–78% are reported herein for the V2O5/SiO2catalysts. Deep oxidation products, CO and CO2, were principally produced over the V2O5/TiO2and V2O5/SnO2catalysts. For the first time,in situRaman analysis clearly showed that for these latter catalysts the surface vanadium(V) oxide species were partially reduced under the steady-state reaction conditions. The performance of the V2O5/TiO2/SiO2catalyst was similar to that of the V2O5/TiO2catalyst, consistent with the earlier observation that vanadia was largely bound to the titania overlayer. It appears that formaldehyde selectivity decreased with increasing catalyst reducibility, but no direct correlation of catalyst activity with reducibility was observed.

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