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Planar transport

The issue of the nonuniform current density is not important for the plate, tubule, and aperiodic architectures shown in Figure 2. The current density in these architectures will be perfectly uniform due to the 1-D nature of transport between anode and cathode. Radial transport occurs in the tubular and aperiodic architecture, while planar transport is operative in the plate architecture (neglecting end effects). [Pg.231]

Only three simple transport geometries are normally encountered planar, cylindrical, and spherical. These are shown in Fig. 13. In planar transport, the flux lines are parallel to each other and normal to the electrode. Cylindrical transport occurs with electrodes that are cylindrical, such as wires, or hemicyclindrical the flux lines converge in the plane which is normal to the cylinder axis but are parallel in planes which include the cylinder axis. Spherical transport is encountered with spherical or hemispherical electrodes, the flux lines being continuations of the radii... [Pg.99]

Of the many complex transport geometries, some of the most important are those encountered with inlaid electrodes (Fig. 14) [25— 30], in which the electrode is planar and embedded in an insulator whose surface is a continuation of the electrode plane. If such an electrode is large, it may be appropriate to treat it as a case of planar transport, with a correction for the edge effect [31, 32], For a small inlaid electrode, however, or for experiments of long duration, such an approximation is no longer valid. [Pg.100]

If the physical meaning of this term is evaluated, in = out. For one-dimensional planar transport (i.e., x direction)... [Pg.75]

For one-dimensional planar transport, substituting Pick s Law for Ja yields... [Pg.76]

Eddy diffusion as a transport mechanism dominates turbulent flow at a planar electrode ia a duct. Close to the electrode, however, transport is by diffusion across a laminar sublayer. Because this sublayer is much thinner than the layer under laminar flow, higher mass-transfer rates under turbulent conditions result. Assuming an essentially constant reactant concentration, the limiting current under turbulent flow is expected to be iadependent of distance ia the direction of electrolyte flow. [Pg.88]

A situation which is frequently encountered in tire production of microelectronic devices is when vapour deposition must be made into a re-entrant cavity in an otherwise planar surface. Clearly, the gas velocity of the major transporting gas must be reduced in the gas phase entering the cavity, and transport down tire cavity will be mainly by diffusion. If the mainstream gas velocity is high, there exists the possibility of turbulent flow at tire mouth of tire cavity, but since this is rare in vapour deposition processes, the assumption that the gas widrin dre cavity is stagnant is a good approximation. The appropriate solution of dre diffusion equation for the steady-state transport of material tlrrough the stagnant layer in dre cavity is... [Pg.108]

Molecular oxygen is transported throughout the body by attaching to the iron(ll) atom in the heme group of hemoglobin. The iron(ll) atom lies at the center of a square planar complex formed by nitrogen atoms. When the O, molecule attaches to the iron, the plane of the heme group becomes distorted. [Pg.789]

Sundararajan, S. andXhakurta, D., Two-Dimensional Wafer-Scale Chemical-Mechanical Planarization Models Based on Lubrication Theory and Mass Transport, Journal of the Electrochemical Society, Vol. 146, No. 2, 1999, pp. 761-766. [Pg.268]

There are many nonintrusive experimental tools available that can help scientists to develop a good picture of fluid dynamics and transport in chemical reactors. Laser Doppler velocimetry (LDV), particle image velocimetry (PIV) and sonar Doppler for velocity measurement, planar laser induced fluorescence (PLIF) for mixing studies, and high-speed cameras and tomography are very useful for multiphase studies. These experimental methods combined with computational fluid dynamics (CFDs) provide very good tools to understand what is happening in chemical reactors. [Pg.331]

In this paper, we report recent progress made In our laboratory In using molecular theory and computer simulation to understand the structure, flow and transport of fluids confined by planar solid walls separated by a few molecular diameters. [Pg.258]

The attractive feature of LADM Is that once the fluid structure Is known (e.g., by solution of the YBG equations given In the previous section or by a computer simulation) then theoretical or empirical formulas for the transport coefficients of homogeneous fluids can be used to predict flow and transport In Inhomogeneous fluid. For diffusion and Couette flow In planar pores LADM turns out to be a surprisingly good approximation, as will be shown In a later section. [Pg.262]

In principle, TPD can also be applied to high-surface area catalysts in plug-flow reactors. Often, however, the curves are seriously broadened by mass-transport phenomena. Hence, the use of single crystals or particles on planar supports offers great advantages for these investigations. [Pg.285]

Schneider A, Colmenaies L, Seidel YE, Jusys Z, Wickman B, Kasemo B, Behm RJ. 2008. Transport effects in the oxygen reduction reaction on nanostructuied, planar glassy carbon supported Pt/GC model electrodes. Phys Chem Chem Phys 10 1931-1943. [Pg.462]

Human skin is the largest organ in the human body. It is fundamentally important to health as the semi-permeable barrier - the first line of defence - between the body and the external world. However, it remains relatively inaccessible to conventional magnetic resonance imaging, firstly because it is thin and therefore requires high spatial resolution, and secondly because it is characterized by relatively short T2 relaxation times, particularly in the outermost stratum comeum. Conventional studies have not usually achieved a resolution better than 70-150 pm, with an echo time of the order of a millisecond or so. As a planar sample, skin has proved amenable to GARField study where it has been possible to use both a shorter echo time and achieve a better spatial resolution, albeit in one direction only. Such studies have attracted the interest of the pharmaceutical and cosmetic industries that are interested in skin hydration and the transport of creams and lotions across the skin. [Pg.101]

Measurements of Pe in fixed-pH solutions but at various different stirring speeds need to be made. The double-reciprocal analysis, HPe versus 1/v , for Caco-2 permeability measurements in the Transwell (Corning Costar) system produced a linear plot for x- 0.8 [514]. The intercept yields the membrane permeability for the particular pH value in the study the slope determines the k constant. From the analysis of testosterone transport, for the stirring speed of 25 rpm (planar rotating shaker), the thickness of each UWL (assuming symmetric geometry) was calculated to be 465 pm at 150 rpm, haq= 110 pm [514], Karlsson and Artursson [512] found x = 1.0 to best represent their stirring-based analysis of the UWL permeability. [Pg.205]

Thus the time during which the transport process attains the steady state depends strongly on the radius of the sphere r0. The steady state is connected with the dimensions of the surface to which diffusion transport takes place and does, in fact, not depend much on its shape. Diffusion to a semispherical surface located on an impermeable planar surface occurs in the same way as to a spherical surface in infinite space. The properties of diffusion to a disk-shaped surface located in an impermeable plane are not very different. The material flux is inversely proportional to the radius of the surface and the time during which stationary concentration distribution is attained decreases with the square of the disk radius. This is especially important for application of microelectrodes (see page 292). [Pg.121]

Convective diffusion to a growing sphere. In the polarographic method (see Section 5.5) a dropping mercury electrode is most often used. Transport to this electrode has the character of convective diffusion, which, however, does not proceed under steady-state conditions. Convection results from growth of the electrode, producing radial motion of the solution towards the electrode surface. It will be assumed that the thickness of the diffusion layer formed around the spherical surface is much smaller than the radius of the sphere (the drop is approximated as an ideal spherical surface). The spherical surface can then be replaced by a planar surface... [Pg.150]

Two-dimensional distributions of ground-state NO were detected by planar laser-induced fluorescence during the process of NO removal in a corona radical shower system in NO/dry air mixtures [57,58], The authors observed that the density of NO molecules decreased not only in the plasma region formed by the corona streamers and the downstream region of the reactor, but also in the upstream region of the reactor. They explained this behaviour by oxidation with ozone, which is transported upstream by electrohydrodynamic flow. [Pg.373]


See other pages where Planar transport is mentioned: [Pg.240]    [Pg.227]    [Pg.475]    [Pg.1172]    [Pg.250]    [Pg.69]    [Pg.287]    [Pg.1243]    [Pg.206]    [Pg.213]    [Pg.471]    [Pg.115]    [Pg.8]    [Pg.60]    [Pg.817]    [Pg.251]    [Pg.257]    [Pg.301]    [Pg.308]    [Pg.108]    [Pg.1428]    [Pg.28]    [Pg.285]    [Pg.21]    [Pg.7]    [Pg.138]    [Pg.155]    [Pg.195]    [Pg.418]    [Pg.564]   
See also in sourсe #XX -- [ Pg.99 ]




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