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Kinetic oxygen atoms

Figure XVIII-2 shows how a surface reaction may be followed by STM, in this case the reaction on a Ni(llO) surface O(surface) + H2S(g) = H20(g) + S(surface). Figure XVIII-2a shows the oxygen atom covered surface before any reaction, and Fig. XVIII-2h, the surface after exposure to 3 of H2S during which Ni islands and troughs have formed on which sulfur chemisorbs. The technique is powerful in the wealth of detail provided on the other hand, there is so much detail that it is difficult to relate it to macroscopic observation (such as the kinetics of the reaction). Figure XVIII-2 shows how a surface reaction may be followed by STM, in this case the reaction on a Ni(llO) surface O(surface) + H2S(g) = H20(g) + S(surface). Figure XVIII-2a shows the oxygen atom covered surface before any reaction, and Fig. XVIII-2h, the surface after exposure to 3 of H2S during which Ni islands and troughs have formed on which sulfur chemisorbs. The technique is powerful in the wealth of detail provided on the other hand, there is so much detail that it is difficult to relate it to macroscopic observation (such as the kinetics of the reaction).
Above pH 9, decomposition of ozone to the reactive intermediate, HO, determines the kinetics of ammonia oxidation. Catalysts, such as WO, Pt, Pd, Ir, and Rh, promote the oxidation of dilute aqueous solutions of ammonia at 25°C, only two of the three oxygen atoms of ozone can react, whereas at 75°C, all three atoms react (42). The oxidation of ammonia by ozone depends not only on the pH of the system but also on the presence of other oxidizable species (39,43,44). Because the ozonation rate of organic materials in wastewater is much faster than that of ammonia, oxidation of ammonia does not occur in the presence of ozone-reactive organics. [Pg.492]

The kinetics of this Uansport, virtually of oxygen atoms tlrrough the solid, is determined by the diffusion coefficient of the less mobile oxide ions, and local... [Pg.162]

The kinetics of this reaction, which can also be regarded as an erosion reaction, shows die effects of adsorption of the reaction product in retarding the reaction rate. The path of this reaction involves the adsorption of an oxygen atom donated by a carbon dioxide molecule on die surface of the coke to leave a carbon monoxide molecule in the gas phase. [Pg.272]

Nickel(IV) complexes react with dimethyl sulphoxide in acidic solution to give the sulphone and nickel(II) ions. The kinetics of this reaction have been studied and found to be very complex in nature. The reaction probably proceeds by initial complexation of the dimethyl sulphoxide to the nickel(IV) species followed by electron transfer and oxygen atom transfer producing the observed products149. [Pg.985]

This oxidation of DMSO is catalyzed by Ag+ cations. Kinetic and infrared spec-trometric evidence fits a mechanism where DMSO coordinates rapidly with Ag+ through its oxygen atom. The oxidation of this complex by Ce4 + then constitutes the slow step. The Ag2+ adduct would then undergo an intramolecular electron transfer in a fast step resulting in the oxidation of DMSO. [Pg.1062]

Based on kinetic investigations the solvolysis of a>-chloroalkyl sulphoxides 506 in 80% ethanol was found to proceed via a cyclic intermediate formed via anchimeric assistance of the sulphinyl oxygen atom . For a solvolysis of 4-halogenothian-l-oxides see Reference 603 (equation 309). [Pg.345]

For potentials higher than 0.5 V vs. RHE, the formation of adsorbed oxygen species at Ru as well as at Pt will block the catalytic surface, leading to a decrease in the methanol adsorption kinetics. Therefore, in a potential range higher than 0.5 V vs. RHE, the kinetics of methanol oxidation is optimized at a Ru-poor catalyst, because methanol adsorption is not blocked and because the presence of Ru provides the extra oxygen atom needed to complete the oxidation of adsorbed CO to CO2. [Pg.352]

Fig. 3.15. Kinetics of conductivity of ZnO film at 20 C during adsorbtion of oxygen atoms 1 - Prior to treatment by zinc vapour 2, 3 - Two consecutive experiments after adsorption of zinc atoms. O-atoms are obtained by pyrolysis of CO2 at P = 0,9 Torr, Tfiiament = lieO -C. Fig. 3.15. Kinetics of conductivity of ZnO film at 20 C during adsorbtion of oxygen atoms 1 - Prior to treatment by zinc vapour 2, 3 - Two consecutive experiments after adsorption of zinc atoms. O-atoms are obtained by pyrolysis of CO2 at P = 0,9 Torr, Tfiiament = lieO -C.
Therefore, the kinetics of generation of defects in surface-adjacent layers is similar to kinetics of emission of O-atoms. (The estimates indicate that the maximum concentration of vacancies in this case may attain the value of 10 for a sample with area 1 cm ). If one assumes that the emission of oxygen atoms is caused by processes of annihilation of vacancies in the sample, then the coincidence in time dependence of stationary concentration of defects can be indicative that these processes are limited by generation of defects, which, in its turn, is controlled by processes of formation of oxide phase in surface-adjacent silver layers. Oxidation, especially at initial stage, is characterized by intensive formation of defects [54]. [Pg.377]

The effect of the aqueous medium on the reactivity and on the stability of the resulting adducts has been investigated to assess which adduct arises from the kinetically favorable path or from an equilibrating process. The calculations indicate that the most nucleophilic site of the methyl-substituted nucleobases in the gas phase is the guanine oxygen atom, followed by the adenine N1, while other centers exhibit a substantially lower nucleophilicity (see activation Gibbs energies in Table 2.2). [Pg.43]

Among the seven reaction pathways, the intramolecular hydrogen abstraction from the methyl group in the MPP radical by the radical peroxy oxygen atom leading to 2-hydroperoxybenzyl radical (HPB, pathways I, Scheme 2.15) is one of the kinetically most favored since its activation enthalpy is only 26.5 kcal/mol. This benzylic radical is fairly unstable and rapidly generate the o-QM by OH radical loss through a very low activation barrier (7.6 kcal/mol). [Pg.58]

Another important catalytic reaction that has been most extensively studied is CO oxidation catalyzed by noble metals. In situ STM studies of CO oxidation have focused on measuring the kinetic parameters of this surface reaction. Similar to the above study of hydrogen oxidation, in situ STM studies of CO oxidation are often conducted as a titration experiment. Metal surfaces are precovered with oxygen atoms that are then removed by exposure to a constant CO pressure. In the titration experiment, the kinetics of surface reaction can be simplified and the reaction rate directly measured from STM images. [Pg.73]

Combined with their kinetic measurements, the authors proposed CO from the gas phase could directly react with oxygen atoms in the surface oxides, accounting for relatively high reactivity of this phase for CO oxidation. This mechanism, termed as Mars-Van Krevelen mechanism, challenges the general concept that CO oxidation on Pt group metals is dominated by the Langmuir-Hinshelwood mechanism, which proceeds via (1) the adsorption of CO and the dissociative adsorption of 02 and (2) surface diffusion of COa(j and Oa(j atoms to ultimately form C02. [Pg.83]


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See also in sourсe #XX -- [ Pg.32 ]




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Kinetics oxygen atoms

Kinetics oxygen atoms

Oxygen atom

Oxygen atomic

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