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Adsorption, and desorption

During Stages II and III the average concentration of radicals within the particle determines the rate of polymerization. To solve for n, the fate of a given radical was balanced across the possible adsorption, desorption, and termination events. Initially a solution was provided for three physically limiting cases. Subsequentiy, n was solved for expHcitiy without limitation using a generating function to solve the Smith-Ewart recursion formula (29). This analysis for the case of very slow rates of radical desorption was improved on (30), and later radical readsorption was accounted for and the Smith-Ewart recursion formula solved via the method of continuous fractions (31). [Pg.24]

Theoretical Approaches to the Kinetics of Adsorption, Desorption, and Reactions at Surfaces... [Pg.439]

Eqs. (1,4,5) show that to determine the equilibrium properties of an adsorbate and also the adsorption-desorption and dissociation kinetics under quasi-equilibrium conditions we need to calculate the chemical potential as a function of coverage and temperature. We illustrate this by considering a single-component adsorbate. The case of dissociative equilibrium with both atoms and molecules present on the surface has recently been given elsewhere [11]. [Pg.444]

Figure 1.5 shows the cumulative pore volume curve for 5-/rm monosized porous PS-DVB particles with 50, 60, and 70% porosity. The curves were drawn by overlapping the measurements from nitrogen adsorption-desorption and mercury intrusion. A scanning electron micrograph of 5-/rm monosized particles with 50% porosity is shown in Fig. 1.6 (87). [Pg.24]

S.W. Jorgensen, N.D.S. Canning, and R.J. Madix, A HREELS, TPD study of nitric oxide adsorption, desorption and reaction on clean and sulfur covered palladium (100), Surf. Sci. 179, 322-350 (1987). [Pg.88]

Parlq)ian P, Anuralqtongsatorn P, Patrick WHJ. 1998. Adsorption, desorption and degradation of a-endosulfan in tropical soils of Thailand. J Environ Sci Health B 33(3) 211-233. [Pg.310]

H2O adsorbs strongly on both Au and Ti02. However, the influence of water on the catalyst or reaction is negligible [2]. PO is known to strongly interact with Ti02, and adsorption, desorption, and decomposition of PO are independent on the presence of gold [3]. [Pg.333]

The Monte Carlo method as described so far is useful to evaluate equilibrium properties but says nothing about the time evolution of the system. However, it is in some cases possible to construct a Monte Carlo algorithm that allows the simulated system to evolve like a physical system. This is the case when the dynamics can be described as thermally activated processes, such as adsorption, desorption, and diffusion. Since these processes are particularly well defined in the case of lattice models, these are particularly well suited for this approach. The foundations of dynamical Monte Carlo (DMC) or kinetic Monte Carlo (KMC) simulations have been discussed by Eichthom and Weinberg (1991) in terms of the theory of Poisson processes. The main idea is that the rate of each process that may eventually occur on the surface can be described by an equation of the Arrhenius type ... [Pg.670]

C1 may be considered as near-ideal tracers for water flow in chaUc. However, and S04 show a more complicated behavior because of ion exclusion, adsorption, desorption, and chemical reactions [186]. [Pg.226]

Acid-base equilibrium is very important to inorganic chemical reactions. Adsorption-desorption and precipitation-dissolution reactions are also of major importance in assessing the geochemical fate of deep-well-injected inorganics. Interactions between and among metals in solution and solids in the deep-well environment can be grouped into four types1 2 3 4 ... [Pg.819]

Analysis of the dynamics of SCR catalysts is also very important. It has been shown that surface heterogeneity must be considered to describe transient kinetics of NH3 adsorption-desorption and that the rate of NO conversion does not depend on the ammonia surface coverage above a critical value [79], There is probably a reservoir of adsorbed species which may migrate during the catalytic reaction to the active vanadium sites. It was also noted in these studies that ammonia desorption is a much slower process than ammonia adsorption, the rate of the latter being comparable to that of the surface reaction. In the S02 oxidation on the same catalysts, it was also noted in transient experiments [80] that the build up/depletion of sulphates at the catalyst surface is rate controlling in S02 oxidation. [Pg.13]

A change in potential can cause any of several effects, including migration of ions into or out of the thin layer, adsorption, desorption, and faradaic reactions consuming or producing species adsorbed on the surface or in solution. For these reasons a difference spectrum (see Eq. (1.3) can exhibit both negative bands due to species formed and positive bands due to species consumed at the sample potential. [Pg.135]

Adsorption, desorption and degradation are simulated in each of the four soil layers (Figure 6). Different parameters can be used in each layer. [Pg.134]

Brununer G.W., Tiller K.G., Herms U., Clayton P.M. Adsorption-desorption and/or precipitation-dissolution processes of zinc in soils. Geoderma 1983 31 337-354. [Pg.333]


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See also in sourсe #XX -- [ Pg.47 ]




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