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Electrode reaction rate constant conditional

A conditional electrode reaction rate constant ) which is defined as the common value of the anodic and cathodic rate constants at the conditional electrode potential is given according to... [Pg.266]

Table 5.1 Conditional electrode reaction rate constants k° and charge transfer coefficients a. (From R. Tamamushi)... [Pg.269]

We assume that neither the preexponential factor of the conditional electrode reaction rate constant nor the charge transfer coefficient changes markedly in a series of substituted derivatives and that the diffusion coefficients are approximately equal. In view of (5.2.52) and (5.2.53),... [Pg.400]

Here kel is the electrode reaction rate constant, Q is the volume per one semiconductor particle (atom or molecule), which leaves the solid and penetrates into the solution, p is the concentration of holes at the interface, p = p X(y,z, t), y, z), and v is the number of holes per one particle dissolved. In the quasistationary case (i.e., when the condition v Lpfrp is satisfied) the distribution of holes is described by the equation similar to Eq. (29) ... [Pg.297]

A detailed examination of the mass transport effects of the HMRDE has been made. At low rotation speeds and for small amplitude modulations (as defined in Section 10.3.6.2) the response of the current is found to agree exactly with that predicted by the steady-state Levich theory (equations (10.15)-(10.17)) [27, 36, 37]. Theoretical and experimental application of the HMRDE, under these conditions, to cases where the electrode reaction rate constant was comparable to the mass-transfer coefficient has also been made [36]. At higher rotation speeds and/or larger amplitude modulations, the observed current response deviated from the expected Levich behaviour. [Pg.396]

The temperature effect often disturbs precise measurements if isothermal conditions cannot be maintained and if it leads to damage of the sample. Equation 1.12 shows that at constant power density the temperature effect decreases with decreasing pulse times. Therefore, the application of short pulses may be of advantage to avoid damages. If, however, the modification of the surface requires a large amount of total energy, it should be delivered with low power density. On the other hand, there are numerous applications of the thermal heating. It can be used to evaporate or to dissociate the substrate (LAMMA) [64], to enhance reaction rates at the surface or the convection of the electrolyte [65-67]. Finally, it can be employed to study electrode reaction rate constants and the dynamics of the double layer [68]. [Pg.10]

According to Eq. (14.2), the activation energy can be determined from the temperature dependence of the reaction rate constant. Since the overall rate constant of an electrochemical reaction also depends on potential, it must bemeasured at constant values of the electrode s Galvani potential. However, as shown in Section 3.6, the temperature coefficients of Galvani potentials cannot be determined. Hence, the conditions under which such a potential can be kept constant while the temperature is varied are not known, and the true activation energies of electrochemical reactions, and also the true values of factor cannot be measured. [Pg.242]

Changes of A from one metal to another, for a given process (e.g. the HER), provide the principal basis for dependence of the kinetics of the electrode process on the metal and are recognized as the origin of electrocatalysis associated with a reaction in which the first step is electron transfer, with formation of an adsorbed intermediate. In the case of the HER, this effect is manifested in a dependence of the logarithm of the exchange current density, I o (i.e., the reversible rate of the process, expressed as A cm , at the thermodynamic reversible potential of the reaction) on metal properties such as 0 (Fig. 2) (14-16, 20). However, as was noted earlier, for reasons peculiar to electrochemistry, reaction rate constants cannot depend on under the necessary condition that currents must be experimentally measured at controlled potentials (referred to the potential of some reference... [Pg.6]

Soon after the discovery of the absorption spectrum of the solvated electron in pulse radiolysis experiments (Chapter 2), the rates and mechanisms of its reaction with a wide variety of solutes was studied. Although it is a transient species, the solvated electron is a very important reducing agent. Indeed, its reduction potential is very negative the value of E°(H2O/e5 ) for the solvated electron in water is equal to -2.8 V with respect to the standard hydrogen electrode. The reaction rate constant and the probability of encounter with another species decide the so-called lifetime ofthe solvated electron, which therefore depends on the experimental conditions. [Pg.43]

As the current density is increased during a metal deposition process (or any electrochemical reaction where the electroactive species in the bulk electrolyte is consumed at the electrode surface) with a constant value of 5 (i.e., for a given forced convection velocity), the surface concentration (CJ decreases since and 5 are constant and independent of the electrode reaction rate. The linear concentration gradient in Equation (26.73) or (26.75) has a maximum value when C = 0. The current density corresponding to this surface concentration condition is known as the limiting current density (1 ) ... [Pg.1759]

In addition to the thermodynamic quantity E°, the electrode reaction is characterized by two kinetic quantities the charge transfer coefficient a and the conditional rate constant k°. These quantities are often sufficient for a complete description of an electrode reaction, assuming that they are constant over the given potential range. Table 5.1 lists some examples of the constant k. If the constant k° is small, then the electrode reaction occurs only at potentials considerably removed from the standard potential. At these potential values practically only one of the pair of electrode reactions proceeds which is the case of an irreversible or one-way electrode reaction. [Pg.268]

The charge transfer reaction (5.2.39) is characterized by the formal electrode potential the conditional rate constant of the electrode reaction kf and the charge transfer coefficient aly while the reaction (5.2.40) is characterized by the analogous quantities E2y kf and a2. If the rate constants of the electrode reactions, which are functions of the potential, are denoted as in Eqs (5.2.39) and (5.2.40) and the concentrations of substances Au A2 and A3 are cly c2 and c3, respectively, then... [Pg.274]

Forced convection can be used to achieve fast transport of reacting species toward and away from the electrode. If the geometry of the system is sufficiently simple, the rate of transport, and hence the surface concentrations cs of reacting species, can be calculated. Typically one works under steady-state conditions so that there is no need to record current or potential transients it suffices to apply a constant potential and measure a stationary current. If the reaction is simple, the rate constant and its dependence on the potential can be calculated directly from the experimental data. [Pg.187]

The formation of water from gaseous hydrogen and oxygen is a spontaneous reaction at room temperature, although its rate may be unobservably small in the absence of a catalyst. At 298.15 K, the heat of the irreversible reaction at constant pressure is — 285,830 J mol . To calculate the entropy change, we must carry out the same transformation reversibly, which can be performed electrochemicaUy with a suitable set of electrodes. Under reversible conditions, the heat of reaction for Equation (6.99) is —48,647 J mol. Hence, for the irreversible or reversible change... [Pg.139]


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See also in sourсe #XX -- [ Pg.257 , Pg.258 ]




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