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Growth kinetically controlled

Flow thins protective film to equilibrium thickness which is a function of both mass transfer rate and growth kinetics. Erosion corrosion rate is controlled by the dissolution rate of the protective film. [Pg.293]

Non-stirred, aerated vessels are used in the process for traditional products such as wine, beer and cheese production. Most of the newly found bioprocesses require microbial growth in an aerated and agitated system. The percentage distribution of aerated and stirred vessels for bioreactor applications is shown in Table 6.1. The performances of various bioreactor systems are compared in Table 6.2. Since these processes are kinetically controlled, transport phenomena are of minor importance. [Pg.142]

A comparative study [10] is made for crystal-growth kinetics of Na2HP04 in SCISR and a fluidized bed crystallizer (FBC). The details of the latter cem be found in [11]. Experiments are carried out at rigorously controlled super-saturations without nucleation. The overall growth rate coefficient, K, are determined from the measured values for the initial mean diameter, t/po, masses of seed crystals before and after growth. The results show that the values for K measured in ISC are systematically greater than those in FBC by 15 to 20%, as can be seen in Table 2. On the other hand, the values for the overall active energy measured in ISC and FBC are essentially the same. [Pg.535]

Curve 1 in Fig. 6.9 shows the influence of constant k, (or of parameters or which are proportional to it) on the current density at constant potential for a reaction with an intermediate value of k°. Under diffusion control (low values of/) the current density increases in proportion to/ . Later, its growth slows down, and at a certain disk speed kinetic control is attained where the current density no longer depends on disk speed. The figure also shows curves for the kinetic current density 4 and the diffusion current density /. [Pg.97]

A more detailed picture of the temperature dependence of the growth is given in Figure 2.4, where the island density is plotted as a function of temperature. It can be seen that only in the temperature range from 207 to 288 K the growth is perfectly template controlled and the number of islands matches the number of available nucleation sites. This illustrates the importance of kinetic control for the creation of ordered model catalysts by a template-controlled process. Obviously, there has to be a subtle balance between the adatom mobility on the surface and the density of template sites (traps) to allow a template-controlled growth. We will show more examples of this phenomenon below. [Pg.33]

The results for Pd and V lead to the conclusion that the high-symmetry sites of the alumina film on Ni3Al(l 1 1) can act as template for the growth of nanostructured model catalysts. They also prove that kinetic control of the growth is of utmost importance. [Pg.48]

Supported model catalysts are frequently prepared by thermally evaporating metal atoms onto a planar oxide surface in UHV. The morphology and growth of supported metal clusters depend on a number of factors such as substrate morphology, the deposition rate, and the surface temperature. For a controlled synthesis of supported model catalysts, it is necessary to monitor the growth kinetics of supported metal... [Pg.85]

Many synthetic methods for the preparation of nanodispersed material have been reported, several routes applying conventional colloidal chemistry, with others involving the kinetically controlled precipitation of nanocrystallites using organometallic compounds.3 6-343 Controlled precipitation reactions yield dilute suspensions of quasi-monodispersed particles. This synthetic method sometimes involves the use of seeds of very small particles for the subsequent growth of larger ones.359 360... [Pg.1050]

Nielsen, A. E. 1964. Diffusion controlled growth. Kinetics of Precipitation. Pergamon Press, Oxford, UK. p. 34. [Pg.230]

Wagner (1961) examined theoretically the growth kinetics of a Gaussian particle size distribution, considering two growth mechanisms. When the process is volume diffusion controlled... [Pg.211]

Kovarova-Kovar, K. and Egli, T. (1998). Growth kinetics of suspended microbial cells from single-substrate-controlled growth to mixed-substrate kinetics, Microbiol. Mol. Biol. Rev., 62, 646-666. [Pg.436]

From the above statements it follows that it should be possible to derive the growth kinetics and calculate the growth rate of uncontaminated electrolyte crystals when the following parameters are known molecular weight, density, solubility, cation dehydration frequency, ion pair stability coefficient, and the bulk concentration of the solution (or the saturation ratio). If the growth rate is transport controlled, one shall also need the particle size. In table I we have made these calculations for 14 electrolytes of common interest. For the saturation ratio and particle size we have chosen values typical for the range where kinetic experiments have been performed (29,30). The empirical rates are given for comparison. [Pg.607]

It is worth reviewing how kinetic and thermodynamic factors generally affect the growth of nanostructures under the influence of surfactants. Though they used CdSe and PbS respectively to study the surfactant-assisted synthesis of nanorods, Peng et al. and Lee et al. have produced a pair of quite complimentary studies. Peng etal. observed that kinetic control via monomer concentration was the principle factor in their growth... [Pg.121]

Gypsum growth rates show a square law dependence on supersaturation with an activation energy of 64 kJ/mol. Growth appears to be surface kinetics controlled. [Pg.310]


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See also in sourсe #XX -- [ Pg.413 ]




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