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Whole oxidation

Palladation of aromatic compounds with Pd(OAc)2 gives the arylpalladium acetate 25 as an unstable intermediate (see Chapter 3, Section 5). A similar complex 26 is formed by the transmetallation of PdX2 with arylmetal compounds of main group metals such as Hg Those intermediates which have the Pd—C cr-bonds react with nucleophiles or undergo alkene insertion to give oxidized products and Pd(0) as shown below. Hence, these reactions proceed by consuming stoichiometric amounts of Pd(II) compounds, which are reduced to the Pd(0) state. Sometimes, but not always, the reduced Pd(0) is reoxidized in situ to the Pd(II) state. In such a case, the whole oxidation process becomes a catalytic cycle with regard to the Pd(II) compounds. This catalytic reaction is different mechanistically, however, from the Pd(0)-catalyzed reactions described in the next section. These stoichiometric and catalytic reactions are treated in Chapter 3. [Pg.14]

Methane oxidations occur only by intermediate and high temperature mechanisms and have been reported not to support cool flames (104,105). However, others have reported that cool flames do occur in methane oxidation, even at temperatures >400 ° C (93,94,106,107). Since methyl radicals caimot participate in reactions 23 or 24, some other mechanism must be operative to achieve the quenching observed in methane cool flames. It has been proposed that the interaction of formaldehyde and its products with radicals decreases their concentrations and inhibits the whole oxidation process (93). [Pg.340]

The net result is that the two electrons lost by the sodium atoms are transferred to the chlorine atoms. Therefore, each of the two equations shown above actually represents one-half of an entire process, which is why they are each called a half-reaction. In other words, an electron won t be lost from a sodium atom without there being a chlorine atom available to pick up that electron. Both halfreactions are required to represent the whole oxidation-reduction process. Halfreactions are useful for showing which reactant loses electrons and which reactant gains them, which is why half-reactions are used throughout this chapter. [Pg.364]

The OH" concentration (earlier thought to be restricted to a thin-surface layer) does in fact extend throughout the whole oxide layer (total thickness 60 A). This fact will prove mechanistically important, as will be seen. [Pg.200]

In the first stage, the potential varies substantially about +0.2 to -0.5 vs. a reference electrode of Hg-HgO. However, thereafter, the curve flattens out and the potential remains constant if the current density is low (e.g., 0.01 mA cm 2) until the reduction reaction to Mn(OH)2 has completed itself throughout the whole oxide mass... [Pg.351]

The consecutive alkenyl mechanism (Figure 3) was put forward as the route for oxidation of unsaturated reactants. The weakly adsorbed intermediates are presumed to be in equilibrium with the gas phase, which enables furan to be seen as a product in butene oxidation (22,24,27). In contrast to the previous work, this study included an examination of the fact that none of the alkene intermediates desorb from the catalyst. It was proposed that the reaction proceeded via more strongly adsorbed alkoxide intermediates that would remain on the surface for the whole oxidation sequence (Figure 5). [Pg.196]

Unlike the previous work, this study examined the fact that none of the alkene intermediates desorb from the surface. Zhang-Iin and coworkers proposed that the reaction proceeded via more strongly adsorbed alkoxide intermediates that would remain on the surface for the whole oxidation scheme (Scheme 12.5). [Pg.528]

Since the delay found in references [4] and [12] concerned the start-up of the whole oxidation plant that included a multi-pass catalytic reactor, the simulations were carried out using the model of the whole plant comprising not only the reactor itself, but also the installations for the recovery of the heat of reaction. For the assumed values of the startup was simulated from the state in which the installation was thoroughly cooled down. The SO2 concentration transients at the outlet of the reactor are shown in Fig. 3. [Pg.515]

It has already been seen that whole oxidation-reduction reactions can be constructed from half-reactions. The direction in which a reaction goes is a function of the relative tendencies of its constituent half-reactions to go to the right or left These tendencies, in turn, depend upon the concentrations of the half-reaction reactants and products and their relative tendencies to gain or lose electrons. The latter is expressed by a standard electrode potential The tendency of the whole reaction to proceed to the right as written is calculated from the Nernst equation, which contains both EP and the concentrations of the reaction participants. These concepts are explained further in this section and the following section. [Pg.292]

This transfer reaction does not influence the whole oxidation kinetics (except for polyenic elastomers), but provides a simple explanation for a relatively high mobility of alkyl radicals and thus for a high 4 value. [Pg.404]

Scientific studies and the ASTM oxidation index standard (ASTM F2102) usually give the quantity of ketones and other carboxyl species present as index of the oxidation degree. It must be pointed out that those ketones, though a product of the oxidative process, do not produce polymeric chain scissions and so they do not result in substantial reduction of the UHMWPE mechanical properties. Quantification of ketones is reliable only if the ratio between ketones and carboxylic acids remains constant through the whole oxidative process [21]. [Pg.315]

Most of the previous studies have used small electrodes (tenths of cm ) in large volumes of solution containing relatively high amounts of reactants the modification of the initial concentrations is thus insignificant and the formation of the intermediate species cannot be followed. In contrast, large area electrodes (tens of cm ) allow the detection of organic species in the bulk of solution by chromatographic methods (HPLC, GC) and also that of the quantity of OH" (or H+) ions involved in the whole oxidation process. [Pg.385]


See other pages where Whole oxidation is mentioned: [Pg.992]    [Pg.735]    [Pg.267]    [Pg.576]    [Pg.326]    [Pg.212]    [Pg.216]    [Pg.38]    [Pg.210]    [Pg.213]    [Pg.735]    [Pg.269]    [Pg.12]    [Pg.56]    [Pg.321]    [Pg.317]    [Pg.334]    [Pg.334]    [Pg.225]    [Pg.376]   
See also in sourсe #XX -- [ Pg.1148 ]




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