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Steady kinetic limiting current

When chemical interactions are not infinitely fast, to determine concentration profiles, it is necessary to solve the set of differential equations containing kinetic terms. Hereinafter the results, obtained with the parameters listed in Table 3.4, are referred to the system of limited lability (LL system). The rate constants were varied so that the relation (3.32) was always obeyed. Current densities applied are given next as fractions of the steady-state limiting current density, that is. [Pg.53]

Similarly to the response at hydrodynamic electrodes, linear and cyclic potential sweeps for simple electrode reactions will yield steady-state voltammograms with forward and reverse scans retracing one another, provided the scan rate is slow enough to maintain the steady state [28, 35, 36, 37 and 38]. The limiting current will be detemiined by the slowest step in the overall process, but if the kinetics are fast, then the current will be under diffusion control and hence obey the above equation for a disc. The slope of the wave in the absence of IR drop will, once again, depend on the degree of reversibility of the electrode process. [Pg.1940]

FIG. 24 Steady-state diffusion-limited current for the reduction of oxygen in water at an UME approaching a water-DCE (O) and a water-NB (A) interface. The solid lines are the characteristics predicted theoretically for no interfacial kinetic barrier to transfer and for y = 1.2, Aj = 5.5 (top solid curve) or y = 0.58, = 3.8 (bottom solid curve). The lower and upper dashed lines denote the... [Pg.322]

Figure 5. Measurement and analysis of steady-state i— V characteristics, (a) Following subtraction of ohmic losses (determined from impedance or current-interrupt measurements), the electrode overpotential rj is plotted vs ln(i). For systems governed by classic electrochemical kinetics, the slope at high overpotential yields anodic and cathodic transfer coefficients (Ua and aj while the intercept yields the exchange current density (i o). These parameters can be used in an empirical rate expression for the kinetics (Butler—Volmer equation) or related to more specific parameters associated with individual reaction steps.(b) Example of Mn(IV) reduction to Mn(III) at a Pt electrode in 7.5 M H2SO4 solution at 25 Below limiting current the system obeys Tafel kinetics with Ua 1/4. Data are from ref 363. (Reprinted with permission from ref 362. Copyright 2001 John Wiley Sons.)... Figure 5. Measurement and analysis of steady-state i— V characteristics, (a) Following subtraction of ohmic losses (determined from impedance or current-interrupt measurements), the electrode overpotential rj is plotted vs ln(i). For systems governed by classic electrochemical kinetics, the slope at high overpotential yields anodic and cathodic transfer coefficients (Ua and aj while the intercept yields the exchange current density (i o). These parameters can be used in an empirical rate expression for the kinetics (Butler—Volmer equation) or related to more specific parameters associated with individual reaction steps.(b) Example of Mn(IV) reduction to Mn(III) at a Pt electrode in 7.5 M H2SO4 solution at 25 Below limiting current the system obeys Tafel kinetics with Ua 1/4. Data are from ref 363. (Reprinted with permission from ref 362. Copyright 2001 John Wiley Sons.)...
However, their simplified analysis offers the interest of a fast criterion about the kinetics control. They considered a Butler-Volmer equation such as Eq. (4-5) where Q and the limiting currents explicitly appear, and expressed the derivative of this steady current with respect to Q (which represents, in fact, the zero frequency limit of the EHD impedance). [Pg.244]

Finding rigorous analytical expressions for the single potential step voltammograms of these reaction mechanisms in a spherical diffusion field is not easy. However, they can be found in reference [63, 64, 71-73] for the complete current-potential curve of CE and EC mechanisms. The solutions of CE and EC processes under kinetic steady state can be found in references [63, 64] and the expression of the limiting current in reference [74], Both rigorous and kinetic steady state solutions are too complex to be treated within the scope of this book. Thus, the analysis of these processes in spherical diffusion will be restricted to the application of diffusive-kinetic steady-state treatment. [Pg.211]

The use of microelectrodes under total steady-state conditions is very advantageous in determining kinetic constants of very fast chemical reactions. To show this, in Fig. 3.28, we show the time influence at different values of rs on the normalized limiting current of a CE mechanism (Eq. 3.249) compared with the time-independent solution (dashed lines and Eq. (3.250)) ... [Pg.214]

Cyclic voltammetry of LaNi03 in the presence of the hexacyanoferrate system and deconvolution of Faradaic and surface processes by means of the RRDE are depicted in Fig. 5. Steady-state results obtained for the hexacyanoferrate redox couple at LaNiO, in alkaline solutions were similar to those reported for La05Sr05CoO3 with very fast kinetics, comparable with the reaction on platinum electrodes, and convective-diffusional limiting currents which obey the Levich equation are observed close to the equilibrium potential (Fig. 5). [Pg.265]

The kinetic behaviour of electrochemical biosensors is most commonly characterized using the dependence of the steady-state amperometric current on the substrate concentration. This type of analysis has some limitations because it does not allow for a decoupling of the enzyme-mediator and enzyme-substrate reaction rates. The additional information required to complete the kinetic analysis can be extracted either from the potential dependence of the steady-state catalytic current or from the shift of the halfwave potential with substrate concentration [154]. Saveant and co-workers [155] have presented the theoretical analysis of an electrocatalytic system... [Pg.97]

Illumination under open-circuit conditions produces electron-hole pairs, which are separated by the potential gradient (see Fig. 3). The concentration of holes increases near the interface, and the concentration of electrons increases near the current collector (curve b in Fig. 4). Under steady-state conditions, the rate of generation of electron-hole pairs is balanced by the rate of homogeneous and interfacial recombination. As the system without kinetic limitations approaches short circuit (curve c in Fig. 4), the concentrations of holes and electrons approach the equilibrium distributions. [Pg.69]

Homogeneous chemical kinetics. A second important application of steady state measurements is in studies of chemical reactivity. Steady state measurements using electrodes of different radii can provide a powerful insight into the kinetics of homogeneous reactions where the limiting current density depends on the magnitude... [Pg.187]

This mode, pioneered by Unwin and coworkers [18], uses the reaction at the tip to perturb an equilibrium at a second interface, by depletion of a component of the solution. The tip current transient is sensitive to the flux of that component as the position of the equilibrium adjusts. The steady state tip current will lie between the values for negative feedback and diffusion-limited positive feedback depending on the kinetics of the equilibrium. If the kinetics are rapid, the same tip current as for a simple redox couple at a metallic substrate is observed. The use of smaller tips and decreased tip/substrate distances results in higher mass transport rates and increases the range of measurable rate constants. [Pg.449]

When mass transport kinetics interferes, the steady-state current-potential curves show a limiting current for the redox process, which brings into play this mass transport. The limiting current is shown on a current-potential curve as a horizontal plateau. It is often also called a limiting diffusion current. It is dependent on the mass transport parameters (migration, diffusion and convection) and is, with a few exceptionsproportional to the concentration of the consumed species, because their mass transport limits the reaction rateand therefore the current flow... [Pg.87]

If first of all we consider the case where the electron transfer is reversible and where the chemical step is very slow, the current will be purely kinetically controlled (i.e. there is no component of diffusion control) and therefore no peaks will be observed on the cyclic voltammogram. Instead a simple steady state type wave will be obtained and the chemical rate constants can be obtained directly from the limiting current using the equation [6]... [Pg.190]


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See also in sourсe #XX -- [ Pg.65 ]




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