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Surface phenomena diffusion

The antiozonant should possess adequate solubiUty and diffusivity characteristics (19). Siace ozone attack is a surface phenomenon, the antiozonant must migrate to the surface of the mbber to provide protection. The antiozonant should have no adverse effects on the mbber processiag characteristics, eg, mixing, fabrication, vulcanization, or physical properties. [Pg.236]

Retention of a given solids particle in the system is on the average veiy short, usually no more than a few seconds. This means that any process conducted in a pneumatic system cannot be diffusion-controlled. The reaction must be mainly a surface phenomenon, or the solids particles must be veiy small so that heat transfer and mass transfer from the interiors are essentially instantaneous. [Pg.1225]

Ozone degradation is a surface phenomenon and hence a physical anti-ozonant must form a protective barrier. A chemical anti-ozonant can be added during polymer fabrication, but again it must diffuse to the surface. It must also provide a defence over the lifetime of the article. [Pg.103]

Uptake is the process by which chemicals (either dissolved in water or sorbed onto sediment and/or suspended solids) are transferred into and onto an organism. For surfactants, this generally occurs in a series of steps a rapid initial step controlled by sorption, where the surface phenomenon is especially relevant then a diffusion step, when the chemical crosses biological barriers, and later steps when it is transported and distributed among the tissues and organs. [Pg.898]

In a more restrictive sense, the term "ion exchange" is used to characterize the replacement of one adsorbed, readily exchangeable ion by another. This circumscription, used in soil science (Sposito, 1989), implies a surface phenomenon involving charged species in outer-sphere complexes or in the diffuse ion swarm. It is not possible to adhere rigorously to this conceptualization because the distinction between inner-sphere and outer-sphere complexation is characterized by a continuous transition, (e.g., H+ binding to humus). [Pg.129]

Problems of Combining Resistances. Suppose that we have found the correct mechanism and resultant rate equation for the surface phenomenon. Combining this step with any of the other resistance steps, such as pore of film diffusion, becomes rather impractical. When this has to be done, it is best to replace the multiconstant rate equation by an equivalent first-order expression, which can then be combined with other reaction steps to yield an overall rate expression. [Pg.381]

Heterogeneous catalysis is a surface phenomenon, therefore the overall kinetic parameters are dependent on the real exposed catalyst surface area. In the supported systems only a part of the photocatalyst is accessible to light and to substrate. Besides, the immobilized catalyst suffers from the surface deactivation since the support could enhance the recombination of photogenerated electron-hole pairs and a limitation of oxygen diffusion in the deeper layers is observed. [Pg.347]

It will be observed that in the results given by Friedmann the water is slightly more dense at the lower depths (300 cm.) than at 50 cm. The waters feeding the Dead Sea are mainly fresh and, being mueh less dense, tend to remain in the surface layers, diffusion taking place relatively slowly. No doubt this accounts for many of the variations observed in the densities of the waters of inland lakes and seas as determined by different investigators who have not usually stated the precise depth at which their samples were taken. This phenomenon is very marked in the case of certain tidal rivers, and has long been known. Mallet, for example, in 1840 drew attention to it in connection with the River Bann in N. Ireland.1... [Pg.224]

The influence of temperature on the occlusion by palladium has also been investigated by Firth.6 He employs the term adsorption to denote the surface phenomenon of rapid occlusion of hydrogen, diffusion not being a determinable factor limits absorption to slow occlusion in which the rate of diffusion or solution is a determinable factor and uses the collective term sorption to include both adsorption and absorption.7 Firth observed adsorption only below 0° C., between 0° and 150° C. he also observed absorption but above 150° C. found absorption only. [Pg.22]

Permeation is a mass transport phenomenon in which molecules transfer through the polymer from one environment to another through diffusive processes. Mass transport proceeds through a combination of three factors in case of polymers. They are (1) dissolution of molecules in polymer (following absorption at the surface), (2) diffusion of molecules through the material, and (3) desorption from the surface of the material (Crank and Park 1968 Kumins and Kwei 1968). [Pg.1164]

Despite the idealized and restrictive set of assumptions, the LSW theory provides a remarkably successful description of many coarsening observations. However, for diffusion-controlled coarsening, it is often found that real systems exhibit a broader and more symmetric steady-state distribution. Furthermore, while the average precipitate size is usually observed to increase qualitatively with the predicted dependence, the rate constant is generally found to be different from that predicted by the LSW theory. For purely reaction-controlled coarsening where the mechanism is strictly a surface phenomenon, the process should be independent of the volume fraction of precipitates as long as the precipitates do not touch. On the other hand, for diffusion control, the interaction of the diffusion fields of the precipitates must be taken into account, and there have been several attempts to incorporate volume fraction effects into the LSW theory (7). [Pg.552]

Diffusion coefficient D) is the ability of the penetrant to move among the polymer segment. It is a kinetic parameter which depends on the polymer segment mobility. Sorption is a surface phenomenon, and it is an indication of the tendency of the penetrant to dissolve into the polymer. Permeation on the other hand, can be considered as the combined effect of sorption and diffusion process. From equation 22.5, it can be inferred that the sorption process controls the permeability. [Pg.552]

Peak diffuseness may be a result of the kinetics of the sorption-desorption process (i.e., slow mass transfer or exchange at sorbent surfaces). Peak diffusion in this case is usually nonsymmetric because the rates of sorption and desorption are not the same. Band spreading due to the final rate of mass exchange is closely related to the diffusion phenomenon. Physical adsorption, for all practical purposes, is instantaneous. The overall process of sorption, however, consists of several parts (a) the movement of sorbate molecules toward the sorbent surface, resulting fi om intergrain diffusion (outer diffusion), (b) movement of sorbate molecules to the inside of pores (i.e., internal diffusion of the sorbate molecules in the pores and surface diffusion in the pores), and (c) the sorption process in general. [Pg.610]

This work demonstrates that PEUU degradation is a surface phenomenon resulting from a classical autooxidation mechanism. By modelling the depth of the surface degraded layer with a diffusion-reaction model, it was shown that PEUU degradation was controlled by diffusion of oxygen into the polymer. 25 refs. [Pg.51]

According to the reactive element effect, the reactive element ion, such as beryllium, diffuses in to the native oxide grain boundaries and prevents the outward diffusion of substrate metal cations (Czerwinski and Smeltzer, 1993 Czerwinski and Szpunar, 1998 Czerwinski, 2000, 2004). The inhibitory effect of boron on aluminum alloy oxidation is clearly a surface phenomenon given the effectiveness of very low levels of boron. This could occur through a combination of boron migration into the MgO lattice and/or boron bonding to the defect-rich MgO surface (Choudhary and Pandit, 1991). [Pg.458]


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See also in sourсe #XX -- [ Pg.3 ]




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