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he process of selective oxidation of o-xylene in a tubular reactor over a vanadia-titania catalyst (V2O5/TiO2) with the catalyst thermal deactivation have been described by means of the Langmuir-Hinshelwood kinetics, while the Erofeev equation for the catalyst deactivation was adopted. On the basis of the model, the kinetic constants have been calculated for eight oxidation reactions from the substrate...
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