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Catalysis particles

The kinetic data are essentially always treated using the pseudophase model, regarding the micellar solution as consisting of two separate phases. The simplest case of micellar catalysis applies to unimolecTilar reactions where the catalytic effect depends on the efficiency of bindirg of the reactant to the micelle (quantified by the partition coefficient, P) and the rate constant of the reaction in the micellar pseudophase (k ) and in the aqueous phase (k ). Menger and Portnoy have developed a model, treating micelles as enzyme-like particles, that allows the evaluation of all three parameters from the dependence of the observed rate constant on the concentration of surfactant". ... [Pg.129]

It would be difficult to over-estimate the extent to which the BET method has contributed to the development of those branches of physical chemistry such as heterogeneous catalysis, adsorption or particle size estimation, which involve finely divided or porous solids in all of these fields the BET surface area is a household phrase. But it is perhaps the very breadth of its scope which has led to a somewhat uncritical application of the method as a kind of infallible yardstick, and to a lack of appreciation of the nature of its basic assumptions or of the circumstances under which it may, or may not, be expected to yield a reliable result. This is particularly true of those solids which contain very fine pores and give rise to Langmuir-type isotherms, for the BET procedure may then give quite erroneous values for the surface area. If the pores are rather larger—tens to hundreds of Angstroms in width—the pore size distribution may be calculated from the adsorption isotherm of a vapour with the aid of the Kelvin equation, and within recent years a number of detailed procedures for carrying out the calculation have been put forward but all too often the limitations on the validity of the results, and the difficulty of interpretation in terms of the actual solid, tend to be insufficiently stressed or even entirely overlooked. And in the time-honoured method for the estimation of surface area from measurements of adsorption from solution, the complications introduced by... [Pg.292]

Free Moisture. The free moisture of a filler is the water present on the surface of the particles. This weakly bound water can sometimes contribute to iaterparticle bonding (reinforcing) or filler—matrix iateraction, ie, biader adsorption or catalysis. A determination of free moisture is usually made by measuriag the percent loss on drying the sample at either 100 or 110°C. [Pg.368]

The proposed mechanism by which chlorinated dioxins and furans form has shifted from one of incomplete destmction of the waste to one of low temperature, downstream formation on fly ash particles (33). Two mechanisms are proposed, a de novo synthesis, in which PCDD and PCDF are formed from organic carbon sources and Cl in the presence of metal catalysts, and a more direct synthesis from chlorinated organic precursors, again involving heterogeneous catalysis. Bench-scale tests suggest that the optimum temperature for PCDD and PCDF formation in the presence of fly ash is roughly 300°C. [Pg.53]

Catalytic properties are dependent on physical form, principally the exposed surface area which is a function of particle size. Industrial PGM catalysts are in the form of finely divided powder, wine, or gauze, or supported on substrates such as carbon or alumina (see Catalysis Catalysts, supported). [Pg.172]

There are only a few weU-documented examples of catalysis by metal clusters, and not many are to be expected as most metal clusters are fragile and fragment to give metal complexes or aggregate to give metal under reaction conditions (39). However, the metal carbonyl clusters are conceptually important because they form a bridge between catalysts commonly used in solution, ie, transition-metal complexes with single metal atoms, and catalysts commonly used on surfaces, ie, small metal particles or clusters. [Pg.169]

Possible role of the induced acidity and basicity in catalysis and environmental chemistry is discussed. The suggested mechanism explains the earlier reported promotive effect of some gases in the reactions catalyzed by Bronsted acid sites. Interaction between the weakly adsorbed air pollutants could lead to the enhancement of their uptake by aerosol particles as compared with separate adsoi ption, thus favoring air purification. [Pg.56]

The identification of particles adsorbed on solid surfaces and recognition of their properties is one of the fundamental problems in research on adsorption and heterogeneous catalysis. Desorption of the adsorbed species from a surface and its subsequent analysis is an important method for solv-... [Pg.343]

A reaction interface is the zone immediately adjoining the surface of contact between reactant and product and within which bond redistributions occur. Prevailing conditions are different from those characteristic of the reactant bulk as demonstrated by the enhanced reactivity, usually attributed to local strain, catalysis by products, etc. Considerable difficulties attend investigation of the mechanisms of interface reactions because this thin zone is interposed between two relatively much larger particles. Accordingly, many proposed reaction models are necessarily based on indirect evidence. Without wishing to appear unnecessarily pessimistic, we consider it appropriate to mention here some of the problems inherent in the provision of detailed mechanisms for solid phase rate processes. These difficulties are not always apparent in interpretations and proposals appearing in the literature. [Pg.109]

Today microemulsions are used in catalysis, preparation of submicron particles, solar energy conversion, extraction of minerals and protein, detergency and lubrication [58]. Most studies in the field of basic research have dealt with the physical chemistry of the systems themselves and only recently have microemulsions been used as a reaction medium in organic synthesis. The reactions investigated to date include nucleophilic substitution and additions [59], oxidations [59-61], alkylation [62], synthesis of trialkylamines [63], coupling of aryl halides [64], nitration of phenols [65], photoamidation of fluoroolefins [66] and some Diels-Alder reactions. [Pg.281]

Sheiko SS, Moller M (2001) Hyperbranched Macromolecules Soft Particles with Adjustable Shape and Capability to Persistent Motion. 212 137-175 Shen B (2000) The Biosynthesis of Aromatic Polyketides. 209 1-51 Shinkai S, see James TD (2002) 218 159-200 Shirakawa E, see Hiyama T (2002) 219 61-85 Shogren-Knaak M, see Imperial B (1999) 202 1-38 Sinou D (1999) Metal Catalysis in Water. 206 41-59... [Pg.238]

A classical issue in transition-metal catalysis is the dependence of catalytic activity on changes in the particle size of the metal clusters in the nanosize region [14]. [Pg.18]

The oxidation of soot is a slow process, owing to its refractory character. Therefore, the soot particles are trapped in a filter, thus increasing the reaction time. However, catalysis is still required. The design of a catalytic filter is a challenge mainly because solid/solid contact is too poor for efficient catalysis [23]. Several ideas have been put forward. [Pg.192]

An important class of materials that originates from the precursor core-shell particles is hollow capsules. Hollow capsules (or shells ) can be routinely produced upon removal of the core material using chemical and physical methods. Much of the research conducted in the production of uniform-size hollow capsules arises from their scientific and technological interest. Hollow capsules are widely utilized for the encapsulation and controlled release of various substances (e.g., drugs, cosmetics, dyes, and inks), in catalysis and acoustic insulation, in the development of piezoelectric transducers and low-dielectric-constant materials, and for the manufacture of advanced materials [14],... [Pg.505]


See other pages where Catalysis particles is mentioned: [Pg.466]    [Pg.466]    [Pg.257]    [Pg.739]    [Pg.2702]    [Pg.2784]    [Pg.2832]    [Pg.1]    [Pg.454]    [Pg.177]    [Pg.180]    [Pg.181]    [Pg.2190]    [Pg.2302]    [Pg.697]    [Pg.29]    [Pg.3]    [Pg.220]    [Pg.778]    [Pg.224]    [Pg.225]    [Pg.681]    [Pg.431]    [Pg.947]    [Pg.489]    [Pg.413]    [Pg.443]    [Pg.113]    [Pg.69]    [Pg.161]    [Pg.279]    [Pg.283]    [Pg.505]    [Pg.522]    [Pg.539]   
See also in sourсe #XX -- [ Pg.833 ]

See also in sourсe #XX -- [ Pg.430 ]




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Catalysis particle size effects

Catalysis/catalysts particle surface

Experimental and theoretical developments in small metal-particle catalysis using electron microscopy

Heterogeneous Catalysis Kinetics in Porous Catalyst Particles

Heterogeneous catalysis particles

Particle surfaces catalysis

Supported metal-particle catalysis

Synthesis with Supported Metal Particles by Use of Surface Organometallic Chemistry Characterization and some Applications in Catalysis

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