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Steady-State Transport

The steady-state solute transport equation can be written as follows  [Pg.83]

Since is the flux density of the adsorbed phase, it can be neglected. Therefore, [Pg.83]


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]

Two equivalent flux expressions define such a steady-state transport model [41]... [Pg.139]

Unlike the previous kinetics imposed by the sink condition, steady-state transport kinetics under non-sink conditions will lead to equilibrium partitioning between the aqueous phase of the donor and receiver compartments and the cell mono-layer. In contrast to the sink condition wherein CR 0 at any time, under nonsink conditions CR increases throughout time until equilibrium is attained. As previously stated in Eqs. (1) and (3), the rate of mass disappearing from the donor solution is... [Pg.252]

Unsteady-state mass transfer caused by excessively fast current or potential ramps. This is especially likely to occur in measurements involving laminar flow past elongated surfaces and in free-convection studies, in which the establishment of secondary flow patterns may require long times. A compromise between the time sufficient to reach steady-state transport and the time necessary to avoid bulk depletion and surface roughening (in metal deposition) is required, and is found most reliably by preliminary experimentation. [Pg.253]

Subotnik JE, Hansen T, Ratner MA, Nitzan A (2009) Nonequilibrium steady-state transport via the reduced density-matrix operator. J Chem Phys 130 144105... [Pg.264]

The steady-state transport of A through the stagnant gas film is by molecular diffusion, characterized by the molecular diffusivity DAg. The rate of transport, normalized to refer to unit area of interface, is given by Fick s law, equation 8.5-4, in the integrated form... [Pg.240]

Neglecting the movement of water relative to the surrounding sediment, we write the steady-state transport equation in one dimension with burial, e.g., in a medium... [Pg.461]

This assumption is based on three relevant indications. First, this wave results in a limiting-current. This means that steady-state transport phenomena control the rate of this reaction, which is not compatible with a possible oxidation of metallic copper to Cu(I) or Cu(II). If the latter were to be valid, a peak-shaped response should have been obtained because of the limited available amount of metallic copper (initially deposited by reduction of Cu(II) or Cu(I) in the reduction wave). In addition, the second voltammetric oxidation wave in the backward scan direction is actually compatible with such a dissolution reaction. [Pg.314]

B. Transport of Gases in Glassy Polymers 1. Steady-State Transport... [Pg.122]

Transient-transport measurements are a powerful tool for evaluating the validity of any sorption-transport model. The ability of a model to predict diffusion time lags is a test for its validity, as all the parameters are fixed by the equilibrium sorption and steady state transport, and because the time lag depends on the specific form of the concentration and diffusion gradients developed during the transient-state experiments. [Pg.124]

All of these simple models have in common the fact that they are accessible to mathematical analysis, while more complex models are not. Yet whether one is dealing with idealized (analyzable) models or complex three-dimensional models, it is essential that the governing equations appropriately represent the underlying physical phenomena. To serve as a resource for this purpose, examples involving time-dependent and steady state transport, simple and facilitated diffusion, and passive permeations between regions were studied. [Pg.219]

Figure 2.3. Steady-state transport of (a) momentum, (b) heat, and (c) mass. Figure 2.3. Steady-state transport of (a) momentum, (b) heat, and (c) mass.
Stucki (1980, 1984) applied the linear nonequilibrium thermodynamics theory to oxidative phosphorylation within the practical range of phosphate potentials. The nonvanishing cross-phenomenological coefficients Ly(i v /) reflect the coupling effect. This approach enables one to assess the oxidative phosphorylation with H+pumps as a process driven by respiration by assuming the steady-state transport of ions. A set of representative linear phenomenological relations are given by... [Pg.568]

These situations, as well as an additional mode of transport known as a surface diffusion, are discussed below. For simplicity, only one-dimensional, steady-state transport is considered. [Pg.43]

The available transport models are not reliable enough for porous material with a complex pore structure and broad pore size distribution. As a result the values of the model par ameters may depend on the operating conditions. Many authors believe that the value of the effective diffusivity D, as determined in a Wicke-Kallenbach steady-state experiment, need not be equal to the value which characterizes the diffusive flux under reaction conditions. It is generally assumed that transient experiments provide more relevant data. One of the arguments is that dead-end pores, which do not influence steady state transport but which contribute under reaction conditions, are accounted for in dynamic experiments. Experimental data confirming or rejecting this opinion are scarce and contradictory [2]. Nevertheless, transient experiments provide important supplementary information and they are definitely required for bidisperse porous material where diffusion in micro- and macropores is described separately with different effective diffusivities. [Pg.86]

Description. The model organism is a free-floating unicellular sphere with characteristics selected, where possible, to match those of a phytoplankton cell. The organism and its environment (Figure Ic) are divided into four concentric zones -the bulk solution, the diffusion layer, the containing membrane and the cell concents. We will assume that the species taken up by the cell is the free metal ion since most of the studies of the uptake of B-subgroup metals by organisms support this hypothesis Z . 5 steady-state transport processes are... [Pg.665]

Penetration of water and low molecular weight nonelectrolytes through the epidermis is proportional to their concentration, and to the partition coefficient of the solute between tissue and vehicle. A form of Pick s law describes steady-state transport through the skin ... [Pg.355]


See other pages where Steady-State Transport is mentioned: [Pg.373]    [Pg.227]    [Pg.547]    [Pg.357]    [Pg.240]    [Pg.253]    [Pg.115]    [Pg.168]    [Pg.157]    [Pg.373]    [Pg.176]    [Pg.233]    [Pg.332]    [Pg.120]    [Pg.90]    [Pg.82]    [Pg.417]    [Pg.161]    [Pg.259]    [Pg.268]    [Pg.212]    [Pg.87]    [Pg.2742]    [Pg.2929]    [Pg.81]    [Pg.83]   


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Steady-state transport equation

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