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Electrochemical consumption mechanism

Only a small selection of the variants in the electrochemical literature can be mentioned here. Thus, impedance techniques (small amplitude sinusoidal perturbation at the electrode with observation of the system s response [22]) as well as polaro-graphic methods (at mercury electrodes) will not be described. Since the notion of a reaction mechanism requires consumption of substance, equilibrium techniques (such as potentiometry) will also not be discussed here. [Pg.7]

Knoth et al. [48] studied the electrochemical behavior of omeprazole with the aid of the direct-current and differential-pulse polarography. Omeprazole was determined in Britton-Robinson buffers pH 7-9 up to a concentration of 10 5 M. The mechanism of the reduction process on the dropping mercury electrode is elucidated. With the consumption of two electrons and two protons, omeprazole will be reduced to 5-methoxy-2-[(3,5-dimethyl-4-methoxypyridin-2-yl)methylthio]-lH-benzimidazole which will be cleaved with the uptake of two further electrons and two protons into 4-methoxy-2,3,5-trimethyl pyridine and 2-mercapto-5-methoxybenz imidazole. [Pg.212]

The electrochemical reduction of oxygen 02 + 2HzO + 4cq -> 40H must be a part of metabolism. The path and rate-determining step depend on the substrate and the pH. However, some mechanisms of the 02 reduction reaction involve 02 (a superoxide ) and it has been suggested (Gerschmann, 1986) that the incomplete consumption of this ion in oxygen reduction allows free 02 to accumulate, adsorb on the surface of cells, reach DNA, and cause destruction of part of it, with the resulting cancer, etc. [Pg.457]

In contrast to active transport, passive transport as a whole does not involve energy consumption and, therefore, only can work down a concentration gradient (or other types of gradients, such as electrochemical potential, thermal, or pressure gradients). In other words, passive transport of molecules equalizes their chemical potential on both sides of the membrane. The process of passive transport can be subdivided into two different mechanisms passive diffusion and facilitated transport. Passive diffusion is a physico-chemical process, whereas in facilitated transport, molecules pass through the membrane via special channels or are translocated via carrier proteins. Both passive diffusion and facilitated transport, in contrast to active transport, follow a gradient, where facilitation merely lowers the activation energy for the transport process. [Pg.1405]

Basically, three mechanisms are responsible for mass transport inside an electrochemical cell diffusion, migration, and convection. Diffusion is mass transport because of concentration gradients, i.e., variations in the concentration of a species with position. Diffusion occurs mainly near the electrode surface because of gradients created by the consumption of species that undergo redox reactions and are incorporated into the deposit. This incorporation process depletes the deposition species near the electrode, generating the concentration gradient. [Pg.826]

Figure 2 also shows this point At steady-state the rate, r< , of consumption of the promoting O species via reaction with C2H4, has to equal its rate of formation I/2F. Consequently, since A=Ar/(I/2F) and Ar=r, it follows A=r/r =TOF/TOF where TOF is the turnover frequency of the catalytic reaction in the NEMCA-promoted state and TOF is the turnover frequency of the reaction of the promoting oxygen species with ethylene. It thus follows for the experiment of Fig. 2 that TOFc=TOF/A=1.3xlO s. This implies that that average lifetime of the promoting species on the catalyst surface is TOF =770 s in excellent qualitative agreement with the catalytic rate relaxation time constant upon current interruption (Fig. 2). This observation provides strong support for the oxygen backspillover mechanism of electrochemical promotion. Figure 2 also shows this point At steady-state the rate, r< , of consumption of the promoting O species via reaction with C2H4, has to equal its rate of formation I/2F. Consequently, since A=Ar/(I/2F) and Ar=r, it follows A=r/r =TOF/TOF where TOF is the turnover frequency of the catalytic reaction in the NEMCA-promoted state and TOF is the turnover frequency of the reaction of the promoting oxygen species with ethylene. It thus follows for the experiment of Fig. 2 that TOFc=TOF/A=1.3xlO s. This implies that that average lifetime of the promoting species on the catalyst surface is TOF =770 s in excellent qualitative agreement with the catalytic rate relaxation time constant upon current interruption (Fig. 2). This observation provides strong support for the oxygen backspillover mechanism of electrochemical promotion.
Alternatively, one may polarize the platinum disk to the quinone-hydroquinone equilibrium potential with the help of a current supplied by an auxiliary circuit. Then one may determine the required current 7, and the rate of consumption of quinone or the rate of formation of hydroquinone. At the quinone-hydroquinone equilibrium potential the electrochemical reduction of hydroquinone vanishes. Consequently, a finite rate of the formation of hydroquinone at the quinone-hydroquinone equilibrium potential equals the partial rate due to the nonelectrochemical mechanism according to Eqs. (VIII.lla)-(VIII.11c). [Pg.370]

Aryl radicals generated electrochemically from halides react with pyrrole and indole. For pyrrole there was a regiochemical preference for 2-substitution ranging from 4 1 to 20 1, while indole gave 3-substitution. <94S366> These reactions are believed to occur by an 5, 1 mechanism and to involve the anions of the heterocyles. The reactions were carried out in liquid ammonia and have the potential to be catalytic rather than stoichiometric in current consumption. [Pg.119]


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Electrochemical mechanism

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