The activation of CH bonds in saturated hydrocarbons is the crucial step in several different types of oxidation reaction on a variety of catalysts and could occur through homolytic or heterolytic mechanisms. From the available evidence it appears that the heterolytic mechanism, with the extraction of a proton, is the most likely process on oxide catalysts and this may also apply to metallic catalysts under typical (oxidising) reaction conditions. However, the state of oxidation of a metallic surface under reaction conditions is complex and the degree of oxidation will depend on the metal, the temperature, the oxygen partial pressure, the metal particle size, the support and the choice of hydrocarbon. The importance of coadsorbates in facilitating the dissociative adsorption of saturated hydrocarbons seems to be well established and could explain the unusual enhancement of activity observed for the oxidation of some saturated hydrocarbons when inorganic gases, such as SO 2, are added to the reaction mixture. The inhibition by products of the oxidation reaction (CO 2 and H 2O) can be quite severe, but H 2O has by far the greatest effect. This is interpreted in terms of an equilibrium involving the formation of surface hydroxide ions which are considered to be inactive for activation of CH bonds. As a consequence, it is possible, especially at low temperatures, that the rate determining step in CH bond activation could be the regeneration of the active sites, through desorption of H 2O, rather than CH bond activation as is commonly assumed. The activation of CH bonds by NO 2 is addressed in the context of selective reduction of NO x by hydrocarbons on various types of oxide catalyst and possible similarities with the promotion of the CH bond activation process by SO 2 are discussed.
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