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Interfadal mechanism

The mechanism of phase transfer catalysis is still a matter of discussion and remains a subject of some controversy. However, it will be roughly classified into two the extraction mechanism proposed by Starks121 and the interfadal mechanism by Makosza1111... [Pg.124]

Park, S.-J., Kim, M.H., Hong, Y.T., and Lee, J.-R. (2001) Surface characteristics of electrochemicaHy modified carbon fibers in phosphoric acid solution effect of surface treatment on interfadal mechanical behaviors of composites. [Pg.208]

With regards to the mechanism of the generation of onium anion, the Starks extraction mechanism and interfacial mechanism (Brandstrom-Montanari modification) are suggested [1-3]. As in the above-described case, the interfadal mechanism seems to be operative in the asymmetric phase-transfer catalysis. [Pg.370]

Figures 8-16 and 8-17 show the state density ZXe) and the exchange reaction current io( ) as functions of electron energy level in two different cases of the transfer reaction of redox electrons in equilibrium. In one case in which the Fermi level of redox electrons cnxEDax) is close to the conduction band edge (Fig. 8-16), the conduction band mechanism predominates over the valence band mechanism in reaction equilibrium because the Fermi level of electrode ensa (= nREDOK)) at the interface, which is also dose to the conduction band edge, generates a higher concentration of interfadal electrons in the conduction band than interfadal holes in the valence band. In the other case in which the Fermi level of redox electrons is dose to the valence band edge (Fig. 8-17), the valence band mechanism predominates over the conduction band mechanism because the valence band holes cue much more concentrated than the conduction band electrons at the electrode interface. Figures 8-16 and 8-17 show the state density ZXe) and the exchange reaction current io( ) as functions of electron energy level in two different cases of the transfer reaction of redox electrons in equilibrium. In one case in which the Fermi level of redox electrons cnxEDax) is close to the conduction band edge (Fig. 8-16), the conduction band mechanism predominates over the valence band mechanism in reaction equilibrium because the Fermi level of electrode ensa (= nREDOK)) at the interface, which is also dose to the conduction band edge, generates a higher concentration of interfadal electrons in the conduction band than interfadal holes in the valence band. In the other case in which the Fermi level of redox electrons is dose to the valence band edge (Fig. 8-17), the valence band mechanism predominates over the conduction band mechanism because the valence band holes cue much more concentrated than the conduction band electrons at the electrode interface.
Gallagher, KJ. Feifknecht,W. Marmweiler, U. (1968) Mechanism of oxidation of magnetite to Y-Fe20j. Nature 217 1118-1121 Gallias, J.L. (1998) Microstructure of the interfacial transition zone around corroded reinforcements. In Katz, A. Benier, M. Alexander, M. Arliguie, G. (eds.) The interfadal transition zone in cementitions composites. E.F.N. Spon, London, 171-178 Galvez, N. Barron,V. Torrent, J. (1999) Preparation and properties of hematite with structural phosphorus. Clays Clay Miner. 47 375-385... [Pg.582]

When surfactants concentrate in an adsorbed monolayer at a surface the interfacial film may provide a stabilizing influence in thin films and foams since they can both lower interfadal tension and increase the interfacial viscosity. The latter provides a mechanical resistance to film thinning and rupture. [Pg.78]

Since tbe polar contribution is tbe most important factor determining the interfadal energy, the polarity of polymers in a dispersed phase strongly influences (i) the adsoiption of sur ctants, (ii) tbe mechanism of particle formation, (in) the particle flocculation, and (iv) the configurational behavior of tbe forming macromolecules. Saveral experimental confirmations of this have been reported elsewhere (Yeliseyeva, 1972). [Pg.250]

Figure 13.15. Mechanism, nomenclature, and constructions for absorption, stripping and distillation in packed towers, (a) Two-fllm mechanism with equiUbrium at the interface, (b) Sketch and nomenclatme for countercurrent absorption or stripping in a packed tower, (c) Equilibrium and material balance lines in absorption, showing how interfadal concentrations are found, (d) Equilibrium and material balance lines in stripping, showing how interfadal concentrations are found, (e) Equilibrium and material balance lines in distillation, showing how interfacial concentrations are found. Figure 13.15. Mechanism, nomenclature, and constructions for absorption, stripping and distillation in packed towers, (a) Two-fllm mechanism with equiUbrium at the interface, (b) Sketch and nomenclatme for countercurrent absorption or stripping in a packed tower, (c) Equilibrium and material balance lines in absorption, showing how interfadal concentrations are found, (d) Equilibrium and material balance lines in stripping, showing how interfadal concentrations are found, (e) Equilibrium and material balance lines in distillation, showing how interfacial concentrations are found.
AuNPs inserted between the electrode surface and redox metalloproteins therefore both work as effective molecular linkers and exert eflfident electrocatalysis. Recent considerations based on resonance turmeling between the electrode and the molecule via the AuNP as a mechanism for enhanced interfadal ET rates suggest that electronic spillover rather than energetic resonance is a hkely origin of the effects (J. Kleis et al., work in progress). Even slightly enhanced spillover compared with a planar Au(lll) surface is enough to enhance the ET rate by the observed amount over a 10-15 A ET distance. [Pg.123]

Microsuspension and Inverse-microsuspension. In suspension polymerizations, particle formation occurs through a droplet breakup-coalescence mechanism, with the diameter controlled by the temperature, interfacial tension, agitation intensity and conversion. Suspension polymerizations have typically been characterized by an initiator soluble in the monomer phase and particle diameters in the 50-1000 pm range [40]. Smaller particles (0.2-20 pm) have been produced at higher agitation speeds (lower interfadal tensions) [41] and in such cases a prefix micro has been added to the nomenclature (microsuspension) to reflect both the dominant synthesis conditions (suspension) and the nominal particle size (1 micron). Therefore, microsuspension polymerization has historically referred to a subdomain of suspension polymerization occurring at smaller particle sizes. Based on an analogy to this nomenclature, inverse-microsuspension polymerization has been proposed for similar water-in-oil... [Pg.127]

The behavior of the pseudoemulsion film is controlled by mechanisms similar to foam films the interfadal rheological properties of the surfactant molecules at low surfactant concentrations and micellar ordering at high surfactant concentrations (i.e., much above the CMC). Not much above the CMC, both of these mechanisms can play a role in film thinning and stability. The stability of a thin pseudoemulsion film also depends on the van der Waals interactions between the phases at the two sides of the film, that is between air and oil, acting across the aqueous film. In a water pseudoemulsion film the Hamaker constant is generally negative, the van der Waals interactions are repulsive and stabilize the film. [Pg.87]

Hydrocarbon-miscible flooding refers to an oil recovery process in which a solvent , usually a mixture of low and intermediate molecular-weight hydrocarbons (methane through hexane), is injected into a petroleum reservoir. Several mechanisms contribute to oil recovery in this process displacement of oil by solvent through the generation of miscibility between solvent and oil, oil swelling with a resulting increase in oil saturation and therefore in oil relative permeability, and reduction of oil viscosity. When solvent and oil remain immiscible, a reduction of gas-oil interfadal tension leads to improved oil recovery. [Pg.261]

In another report a semi-empirical rate eqtiation has been proposed combining mechanisms of homogeneous catalysis and interfadal parameters for biphasic hydroformylation of 1-dodecene with a water-soluble Rh complex catalyst [40]. [Pg.160]

From the previous discussion, we have seen that real focus for the discussion of the microscopies of the Schottky barrier is understanding the mechanisms which determine the interfadal layer. The interplay of a variety of effects... [Pg.100]

Molecules or groups of atoms (ions) behaving as permanent dipoles may have considerable inertia, so relaxation frequencies for orientation polarization may be expected to occur at relatively smaller frequencies, as in the radio-frequency range. Since the alternation of interfadal polarization requires a whole body of charge to be moved through a resistive material, the process maybe slow. The relaxation firequency for this mechanism is thus low, occurring at about 10 Hz. [Pg.352]

For the thermal interaction, the force is sometimes identified as the temperature with its generalized coordinate being the entropy [8]. Such an identification provides an obvious and appealing symmetry because it makes thermal interactions appear to be structurally analogous to nonthermal interactions however, we prefer not to make such an identification because for all known nonthermal interactions the generalized coordinate can be measured, whereas entropy cannot. In this book we will consider only mechanical, gravitational, interfadal, and chemical forces plus the thermal interactions others will not be used. [Pg.16]

The making of an emulsion involves many nonequilihrium features, at least from the mechanical point of view. Actually the product of the interfadal tension by the produced surface area y AA. which is the inlerfacial energy, is always much smaller than the mechanical energy put into the system by the stirring device. A signiheani characteristic is the way and the efficiency in which the energy is provided to the drop so that breaking is favored over coalescence. This has to do not only with the device but with formulation and eventual transient events. [Pg.25]

The thickness of interfadal transition zone is determined by the range of oriented portlandite crystals and equals 50-100 pm [16]. However, only a 10-20 pm thick layer of this zone shows clearly different mechanical properties, as compared to the bulk cement matrix. The microstmcture of interfacial transition zone is variable and depends on the type and properties of cement and reinforcement, presence of admixtures, concrete maturing regime, as well as the other factors (Fig. 6.19). [Pg.386]

Hasegawa, N. Okamoto, H. Kato, M. Usuki, A. (2000) Preparation and Mechanical Properties of Polypropylene-Clay Hybrids based on Modified Polypropylene and Organophilic Clay. /. Aypl. Polym. Sci. Vol.78, No.ll, p>p.l918-1922 Huxtable, S. Cahill, D. Shenogin, S. Xue, L. Ozisik, R. Barone, R Usrey, M. Strano, M. Siddons, G. Shim, M. Keblinski, P. (2003) Interfadal Heat Flow in Carbon Nanotube Suspensions. Nat. Mater. Vol.2, No.ll, pp.731-734 Hyatt, J. (1984) Liquid and Supercritical Carbon Dioxide as Organic Solvents. J. Org. Chem. Vol.49, No.26, pp.5097-5101... [Pg.387]

Park, J.-M., Kim, D.-S. and Kim, S.-R. (2003) Interfadal properties and microfailure degradation mechanisms of bioabsorbable fibers/poly-L-lactide composites using micromechanical test and nondestructive acoustic emission. Composites Science and Technology, 63, 403 19. [Pg.238]


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See also in sourсe #XX -- [ Pg.124 ]




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