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Electrode segmentation

The main problem, the height-dependent differential pressure between the catho-lyte gap and oxygen across the ODC, could be solved with the pressure compensation system based on oxygen supply via gas pockets [1] (see Fig. 4.2). The first successful piloting was done in October 1995 on the basis of Bayer engineering and construction. In a four-gas-pocket element with each electrode segment of 180 x 180 mm2 individually supplied with power, the proper function of pressure compensation could be proven for a total height of 90 cm. [Pg.63]

Figure 5.17 Cumulative probability distribution for the occurrence of the nucleation coordinates of Fig. 5.16 in electrode segments along one of the coordinates, or y, respectively [5.22]. Figure 5.17 Cumulative probability distribution for the occurrence of the nucleation coordinates of Fig. 5.16 in electrode segments along one of the coordinates, or y, respectively [5.22].
Electrode segmentation into strips and square pixels of size 100 pm - 1 mm (see Fig. 5). [Pg.133]

Fig. 13. Schematic diagram of a fluorescence activated LCD. The abbreviations are Reflector RC, Notch N, Fluorescent plate FP, Dispersing pattern DP, Fluorescence light FL, Electrode segment ES, Polarizer P, Ambient light AL. Fig. 13. Schematic diagram of a fluorescence activated LCD. The abbreviations are Reflector RC, Notch N, Fluorescent plate FP, Dispersing pattern DP, Fluorescence light FL, Electrode segment ES, Polarizer P, Ambient light AL.
Fig. 5. Linear MHD generator configurations (a), two-terrninal Faraday or continuous electrode (b), segmented Faraday (c), diagonal connections and... Fig. 5. Linear MHD generator configurations (a), two-terrninal Faraday or continuous electrode (b), segmented Faraday (c), diagonal connections and...
In practice, elimination of axial current flow requires relatively fine segmentation, eg, 1—2 cm, between electrodes, which means that a utihty-sized generator contains several hundred electrode pairs. Thus, one of the costs paid for the increased performance is the larger number of components and increased mechanical complexity compared to the two-terrninal Faraday generator. Another cost is incurred by the increased complexity of power collection, in that outputs from several hundred terminals at different potentials must be consoHdated into one set of terminals, either at an inverter or at the power grid. [Pg.416]

This equation reflects the rate of change with time of the concentration between parallel planes at points x and (x + dx) (which is equal to the difference in flux at the two planes). Fick s second law is vahd for the conditions assmned, namely planes parallel to one another and perpendicular to the direction of diffusion, i.e., conditions of linear diffusion. In contrast, for the case of diffusion toward a spherical electrode (where the lines of flux are not parallel but are perpendicular to segments of the sphere), Fick s second law has the form... [Pg.6]

Figure 51. Arrhenius plot of ln 1/(3 [ Q t)ldt2]) from data corresponding to Fig. 54. The conformational energy consumed per mole of polymeric segments in the absence of any external electric field (AH) can be obtained from the slope. (Reprinted from T. F. Otero and H.-J. Grande, Reversible 2D to 3D electrode transition in polypyrrole films. Colloid Surf. A. 134, 85, 1998, Figs. 4-9. Copyright 1998. Reproduced with kind permission of Elsevier Science-NL, Sara Burgerhartstraat 25, 1055 Amsterdam, The Netherlands.)... Figure 51. Arrhenius plot of ln 1/(3 [ Q t)ldt2]) from data corresponding to Fig. 54. The conformational energy consumed per mole of polymeric segments in the absence of any external electric field (AH) can be obtained from the slope. (Reprinted from T. F. Otero and H.-J. Grande, Reversible 2D to 3D electrode transition in polypyrrole films. Colloid Surf. A. 134, 85, 1998, Figs. 4-9. Copyright 1998. Reproduced with kind permission of Elsevier Science-NL, Sara Burgerhartstraat 25, 1055 Amsterdam, The Netherlands.)...
A simplified Pourbaix diagram for the zinc electrode at pH between 0 and 14 is shown as an example in Fig. 3.1. The vertical axis is that of the values of electrode potential on the SHE scale for activities of the Zn + and HZnO ions of 1 mol/kg. The segments of solid lines correspond to the equilibrium potentials of the following electrode reactions ... [Pg.49]

Polarization equations of the type (14.35) or (14.38) contain the mean values of true current density. However, the rate-determining step is more often concentrated at just a few segments of the electrode the true working area changes continuously and an exact determination of this area is practically impossible. This gives rise to difficulties in an interpretation of polarization data. [Pg.260]

Structural surface inhomogeneity influences the anodic dissolution process in the case of metals with appreciable activation polarization. As a rule, segments with perturbed structure dissolve more rapidly than ordered segments. In a number of cases this causes crystallites to break away from the electrode surface and form metal sludge. [Pg.300]


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Electrodes segmented

Electrodes segmented

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