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Quantitative treatment, interfacial

The quantitative treatment for i as a function of a varying T f was first solved analytically by Sevdk in 1948. The solution involves Laplace transformation and the error function complement expressions applied in Vol. I, Section (4.2.11). It is better to quote here the rather simpler equations that can be found if one takes the entire surface as available for the exchange of electrons, i.e., the easy case of 0 = 0. Then (Gileadi, 1993),22 with this assumption, the peak potential is related to the rate constant (Ay) for the interfacial reaction, to the Tafel constant b, and to the sweep rate s, by the equation ... [Pg.715]

The quantitative treatment of surface phenomena involves an important uncertainty. It is convenient to regard the interface between two phases as a mathematical plane, such as SS in Figure 4.12. This approach, however, is unrealistic, especially if an adsorbed film is present. Not only will such a film itself have a certain thickness, but also its presence may influence nearby structure (for example, by dipole-dipole orientation, especially in an aqueous phase) and result in an interfacial region of varying composition with an appreciable thickness in terms of molecular dimensions. [Pg.80]

Similar experiments with dual radioisotopic labeling show that there is a small manganese(II) ion excess in the manganese(II) ion/calcium-montmorillonite (labeled with 54Mn and 45Ca isotopes) interfacial reaction. It means that there is an adsorption reaction besides ion exchange, but it has a very low contribution. For this reason, the presence of adsorption can be observed, but its quantitative treatment is difficult. [Pg.106]

Extended interfacial regions—Characterization and quantitative treatment of three-dimensional porous electrodes is essential for the... [Pg.114]

Marcia-Rio et al. used this W/O AOT microemulsion as the medium for nitroso transfer to secondary amines from A-methyl-/V-nitroso-/ -toluenesulfonamide (8). Their quantitative treatment, which includes consideration of reactant solubilities, shows that reaction occurs at the microemulsion interface, where it is slower than in water. This rate difference is understandable on the very reasonable assumption that the polarity of the microemulsion interface is lower than that of water [99-101]. These kinetic data indicate that the interfacial regions of the water pool microdroplets in O/W microemulsions and reverse micelles can be regarded as reaction media corresponding to descriptions applied to normal aqueous association colloids. This concept has also been applied to acid-base equilibria, especially by El Seoud and his group [112,116,117]. [Pg.471]

In volume 1 (Chapters 4 and 5) a fairly detailed treatment of the movement and transport of ions was presented qualitative pictures and quantitative accounts were given of the diffusion and electrical migration of ions in the bulk of the electrolyte. In the treatment of electrodic processes, no mention was made at first of a connection between the transport in solution and processes at electrodes. It was then realized that this neglect of ion transport in solution (ionics) was tantamount to assuming that at no stage in the course of a charge-transfer reaction did the interfacial concentrations of electron acceptors and donors depart from their bulk values. [Pg.537]

Two different polyacrylonitrile precursor carbon fibers, an A fiber of low tensile modulus and an HM fiber of intermediate tensile modulus were characterized both as to their surface chemical and morphological composition as well as to their behavior in an epoxy matrix under interfacial shear loading conditions. The fiber surfaces were in two conditions. Untreated fibers were used as they were obtained from the reactors and surface treated fibers had a surface oxidative treatment applied to them. Quantitative differences in surface chemistry as well as interfacial shear strength were measur-ed. [Pg.21]

Kinetic data obtained under these conditions have been fitted by pseudophase models in terms of k by solving the PBE or in terms of k / Vm by using the PIE model [10], However, because these treatments contain reasonable but unproven assumptions [64] and because values of parameters such as //, V, and are only approximate, values of k may not be unique [123], Extensive evidence shows that k kw for many reactions of anionic nucleophiles, but this generalization does not hold for anionic electrophiles [83,124,125], Therefore, although a great many kinetic data are consistent with the assumption that counterions concentrate at surfaces of ionic association colloids, it is difficult to obtain quantitative estimates of interfacial ion concentrations from measured rate constants. [Pg.472]

In subsequent treatments, Teramoto et al (25, 26) developed an analysis of both semi-batch and continuous reactor performance which incorporated a quantitative discrimination of the role of film and bulk reaction. The intractability of the non-linear product terms in the diffusion/reaction equations was ultimately avoided by a linearisation method, identical to that proposed by Hikita and Asai (22). In this approach the profiles Co(x) and Cg(x) are replaced by their interfacial values, so t t the diffusion/reaction equations become... [Pg.266]

Adhesion is an interfacial phenomenon that occurs at the interfaces of adherends and adhesives. This is the fact underlying the macroscopic process of joining parts using adhesives. An understanding of the forces that develop at the interfaces is helpful in the selection of the right adhesive, proper surface treatment of adherends, and effective and economical processes to form bonds. This chapter is devoted to the discussion of the thermodynamic principles and the work of adhesion that quantitatively characterize the surfaces of materials. Laboratory techniques for surface characterization have been described which allow an understanding of the chemical and physical properties of material surfaces. [Pg.21]

Thus, the proposed in the present work stmetnral (fractal) treatment explains quantitatively the coke lesidne formation process at eomposites HDPE/Al(OH)3 combustion. The antipyrene (in the considered case - Al(OH)3) decomposition is realized in the surface (interfacial) layers of fractal aggregates, formed by Al(OH)j particles in their aggregation process. This process in the given case is due to the indicated layers friable structure that allows an easy access to them the air, necessary for decomposition. [Pg.227]

The occurrence of one or the other of these processes will depend on a delicate balance between the tensile properties of the adhesive and the interfacial parameter, Despite the fact that the level of stress and the maximum extension that these fibrils will achieve often controls the amount of work necessary to debond the adhesive (the external work done during this process can sometimes represent up to 80% of the practical debonding energy), no quantitative analytical treatment of this extension and fracture process exists for such highly non-linear materials. Numerical methods have, however, been successful in predicting at least the extensional behavior if not the point of fracture [29,30]. [Pg.544]


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