The performance of the active catalyst 5%V2O5-l.9%MgO/TiO2 in propane oxidative dehydrogenation is investigated under various reactant contact modes: co-feed and redox decoupling using fixed bed and co-feed using fluid bed. Using fixed bed reactor under co-feed conditions, propane is activated easily on the catalyst surface with selectivities ranging from 30 to 75% depending on the degree of conversion. Under varying oxygen partial pressures, especially for higher than the stoichiometric ratio O-2/C3H8 = 1/2, nor the propane conversion or the selectivities to propene and COx are affected. The performance of the catalyst in the absence of gas phase oxygen was tested at 400 degrees C. It was confirmed that the catalyst surface oxygen participates to the activation of propane forming propene and oxidation products with similar selectivities as those obtained under co-feed conditions. The ability of the catalyst to fully restore its activity by oxygen treatment was checked in repetitive reduction-oxidation cycles. Fluid bed reactor using premixed propane-oxygen mixtures was also employed in the study. The catalyst was proved to be very active in the temperature range 300-450 degrees C attaining selectivities comparable to those of fixed bed. (C) 2007 Elsevier B.V. All rights reserved.