The Pt/V 2 O 5 and Pd/V 2 O 5 systems formed upon hydrogen reduction have catalytic activity in the oxidation of carbon monoxide exceeding the activity of Pt/Al 2 O 3 and Pd/Al 2 O 3 . The transition from the low-activity to high-activity state on the Pt/V 2 O 5 and Pd/V 2 O 5 catalysts is characterized by temperature hysteresis and change in the kinetic equation. X-ray phase analysis (XPA), X-ray photoelectron spectroscopy (XPES), and X-ray spectral microanalysis were used to establish that prior reduction of V 2 O 5 by hydrogen gives VO 2 , V 6 O 13 , a-H x V 2 O 5 , and b-H x V 2 O 5 , which facilitates the formation of an active catalyst surface.The catalytic oxidation of carbon monoxide holds considerable interest since it is the basis of exhaust gas pollution control technology. The oxidation of carbon monoxide on platinum and palladium supported on Al 2 O 3 and SiO 2 , which are inert in this reaction, has been studied in detail. However, as noted by Rozovskii et al. [1], despite many studies, the nature of the processes occurring on the catalyst surface is still unclear. We should note that platinum metals supported on transition metal oxides participate in the formation of the catalyst surface layer, facilitating the reduction of the oxides by gaseous reducing agents, in particular, hydrogen [2,3].In previous work [4,5], we studied the oxidation of small molecules (H 2 , CO, CH 4 ) on platinum and palladium supported on Group-V and Group-VI 4d-and 5d-metal oxides and found that compounds facilitating the formation of active catalysts are generated due to prior hydrogen reduction of the oxides studied.In the present work, we studied the effect of platinum and palladium additives on the state of the surface layer of vanadium oxides formed upon hydrogen reduction and the catalytic activity of the systems obtained in the oxidation of CO.The oxidation of CO on catalysts Pd/V 2 O 5 and Pt/V 2 O 5 was studied by Chashechnikova [6] and Kosaki [7], respectively, without comparison with the activity of Pt/Al 2 O 3 and Pd/Al 2 O 3 systems. We should note that the state of the surface layer of Pt/vanadium oxide and Pd/vanadium oxide catalysts formed upon reduction in hydrogen has not been sufficiently studied and the reasons for the high activity of these catalysts in the oxidation of CO have not been fully revealed.The catalytic activity of the samples was measured in a flow reactor at atmospheric pressure. The flow rate of the reaction mixture was 0.1 L/min. The catalyst charge was 1 g. The reaction components (CO, CO 2 , and O 2 ) were analyzed chromatographically. The reaction mixture contained 2% CO, 20% O 2 , and 78% He. The reaction kinetics was studied in a 126 0040-5760/10/4602-0126