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Deactivators identifying

Do we expect this model to be accurate for a dynamics dictated by Tsallis statistics A jump diffusion process that randomly samples the equilibrium canonical Tsallis distribution has been shown to lead to anomalous diffusion and Levy flights in the 5/3 < q < 3 regime. [3] Due to the delocalized nature of the equilibrium distributions, we might find that the microstates of our master equation are not well defined. Even at low temperatures, it may be difficult to identify distinct microstates of the system. The same delocalization can lead to large transition probabilities for states that are not adjacent ill configuration space. This would be a violation of the assumptions of the transition state theory - that once the system crosses the transition state from the reactant microstate it will be deactivated and equilibrated in the product state. Concerted transitions between spatially far-separated states may be common. This would lead to a highly connected master equation where each state is connected to a significant fraction of all other microstates of the system. [9, 10]... [Pg.211]

The typical industrial catalyst has both microscopic and macroscopic regions with different compositions and stmctures the surfaces of industrial catalysts are much more complex than those of the single crystals of metal investigated in ultrahigh vacuum experiments. Because surfaces of industrial catalysts are very difficult to characterize precisely and catalytic properties are sensitive to small stmctural details, it is usually not possible to identify the specific combinations of atoms on a surface, called catalytic sites or active sites, that are responsible for catalysis. Experiments with catalyst poisons, substances that bond strongly with catalyst surfaces and deactivate them, have shown that the catalytic sites are usually a small fraction of the catalyst surface. Most models of catalytic sites rest on rather shaky foundations. [Pg.171]

A mixture of 9.05 g (0.05 mol) of bcnzaldchydc anilide and 7.87 g (0.07 mol) of potassium /-butoxidc in 200 mL of DMb is cooled to —40 C under N2. This mixture is stirred and maintained at this temperature while a solution of 10.47 g (0.07 mol) of 2-chloro-Ar,/V-diethylacetamide in 125 mL of l)MF. is added over a 2-hr period. The reaction is allowed to warm to r.t. over a 30-min period and concentrated to a small volume in vacuo at 35 C. The residue is diluted with H20 and Et,0. After removal of the Ei20 layer, the aqueous fraction is extracted with another two portions of Er2(), and the combined extracts are dried over MgS04. Filtration and evaporation gives 16.32 g of crude material. This material is chromatographed on deactivated alumina with initial elution with pet. ether followed by benzene. Two pure fractions are obtained which, after reciystalli/.aiiou from ben/ene/pet. ether, are identified as the (ranj-isomer 3a yield 1.03 g (7%) mp 90-92eC. and the cts-isomer 3b yield 8.53 g (58%) mp 80.5-82.5cC. [Pg.763]

It is seen that to identify the impurities, the column appeared to be significantly overloaded. Nevertheless, the impurities were well separated from the main component and the presence of a substance was demonstrated in the generic formulation that was not present in the Darvocet . The mobile phase was 98.5% dichloromethane with 1.5% v/v of methanol containing 3.3% ammonium hydroxide. The ammoniacal methanol deactivated the silica gel but the interaction of the solutes with the stationary phase would still be polar in nature. In contrast solute interactions with the methylene dichloride would be exclusively dispersive. [Pg.307]

Figure 1 shows the effects of reaction temperature on the conversions of CO2 and CH4 over Ni-YSZ-Ce02 and Ni-YSZ-MgO catalysts. It was found that the Ni-YSZ-Ce02 catalyst is showed higher catalytic activity than the Ni-YSZ-MgO catalyst at temperature range of 650 850 Ti and the maximum activity was observed at above 800 °C, the optimum temperature for internal reforming in SOFC system [5]. In our previous work, it was identified that Ni-YSZ-MgO catalyst was deactivated with reaction time, however Ni-YSZ-Ce02 showed stable catalytic activity more than Ni-YSZ-MgO catalyst imder tiie tested conditions [6]. [Pg.615]

GL 18] ]R 1] ]P 19a] For a sputtered palladium catalyst, low conversion and substantial deactivation of the catalyst were foimd initially (0.04 mol 1 60 °C 4 bar 0.2 ml min ) [60, 62]. Selectivity was also low, side products being formed after several hours of operation (Figure 5.25). After an oxidation/reduction cycle, a slightly better performance was obtained. After steep initial deactivation, the catalyst activity stabilized at 2-4% conversion and about 60% selectivity. After reactivation, the selectivity approached initially 100%. As side products, all intermediates except phenylhydroxylamine were identified. [Pg.627]

The liquid-liquid interface has been identified as the major factor responsible for papain deactivation in a biphasic system [66]. If the interfacial tension can be decreased to a small value using surfactant, the biocatalyst stability will be expected to increase. [Pg.560]

By decreasing the GHSV values, the selectivity dramatically decreased due to the presence of the side-reaction of C-alkylation on the aromatic ring, giving rise to relevant amounts of 3-MC and a not-fully-identified methyl-MDB derivative (however, the 3-methyl isomer is the most probable candidate). Lastly, the lowest GHSV value was conducive to the condensation of PYC, with a formation of heavy by-products, a dramatic decrease of C-balance, and resulting catalyst deactivation. [Pg.350]

This same [e] experimental protocol leads to a graphical overlay plot that yields valuable kinetic information if the two experiments described in Table 50.1 are plotted together as reaction rate vs. [2], the two curves will fall on top of one another ( overlay ) over the range of [2] common to both only if the rate is not significantly influenced by changes in the overall catalyst concentration within the cycle, including catalyst activation, deactivation or product inhibition. Overlay in same excess plots, therefore, may be used to confirm catalyst robustness or identify problems such as catalyst deactivation or product inhibition. [Pg.453]

Figura 2.9 Dse of th Grob test Mixture to compare tbe activity of various glass surfaces coated with ov-ioi. Surface types A > Untreated pyrex glass, B pyrex glass deactivated by thermal degradation of Ceurbowax 20M, C < SCOT column, prepared with Silanox 101, D pyrex glass column coated with a layer of barium carbonate and deactivated as in (B), and E - untreated fused silica. Components are identified in Table 2.7 with ac - 2-ethylhexanoic acid. (Reproduced with permission from ref. 152. Copyright Elsevier Scientific Publishing Co.)... Figura 2.9 Dse of th Grob test Mixture to compare tbe activity of various glass surfaces coated with ov-ioi. Surface types A > Untreated pyrex glass, B pyrex glass deactivated by thermal degradation of Ceurbowax 20M, C < SCOT column, prepared with Silanox 101, D pyrex glass column coated with a layer of barium carbonate and deactivated as in (B), and E - untreated fused silica. Components are identified in Table 2.7 with ac - 2-ethylhexanoic acid. (Reproduced with permission from ref. 152. Copyright Elsevier Scientific Publishing Co.)...
Contact of aqueous ethylene glycol solutions with d.c.-energised silvered copper wires causes ignition of the latter. Bare copper or nickel- or tin-plated wires were inert and silver-plated wire can be made so by adding benzotriazole as a metal deactivator to the coolant solution [1], This problem of electrical connector fires in aircraft has been studied in detail to identify the significant factors [2],... [Pg.349]

The most commonly accepted model for the hydrogen-acceptor pairs locates H at the BC site (see Fig. 4). This model was originally proposed for the H—B complex on the basis of satisfied bonds to explain the increased resistivity (Pankove et al., 1983), SIMS profiles (Johnson, 1985), and a hydrogen local-mode frequency consistent with a perturbed hydrogen-silicon bond (Pankove et al., 1985 Johnson, 1985 Du et al., 1985). The acceptor deactivation by atomic hydrogen was subsequently observed for Al, Ga, and In acceptors in silicon (Pankove et al., 1984). Hydrogen local-mode vibrations were identified as well for the H—Al and H—Ga complexes (Stavola et al., 1987). The boron vibrational frequency for the H—B pair was first identified by Stutzmann (1987) and Herrero and Stutzmann (1988a). [Pg.543]

This catalytic cycle, generating acetyl iodide from methyl iodide, has been demonstrated by carbonylation of anhydrous methyl iodide at 80°C and CO partial pressure of 3 atm using [(C6H5)4As][Rh(CO)2X2] as catalysts. After several hours reaction, acetyl iodide can be identified by NMR and infrared techniques. However, under anhydrous conditions some catalyst deactivation occurs, apparently by halogen abstraction from the acetyl iodide, giving rhodium species such as frans-[Rh(CO)2I4] and [Rh(CO)I4] . Such dehalogenation reactions are common with d8 and d10 species, particularly in reactions with species containing weak... [Pg.260]

Chen et al,33 studied the deactivation of Zr02-promoted cobalt on silica in the FTS using a fixed bed reactor at realistic reaction conditions and high conversions (65-90%). A fraction of the lost activity was regained by a re-reduction, and the selectivity was reported to be unaffected by deactivation and regeneration. The authors identified hydrated cobalt silicates using IR and XRD analyses, and suggested that these species caused the permanent deactivation. [Pg.16]

In terms of the effect of water on the deactivation, several mechanisms have been identified, and they will influence the stability of the catalyst depending on the conditions and the support used. At high partial pressures of water oxidation is always a possibility, but the various reports are less clear to whether this is mainly surface oxidation of cobalt particles irrespective of particle size, or if small particles... [Pg.24]

The authors ascribed the high WGS rates of the Pt/FSM-16 catalysts to confinement effects which increased the activities of Pt surface atoms, as well as to anisotropic morphological effects. Based on infrared studies, the authors identified unidentate formate species as intermediates in Au/NaY, and though the species was also observed on Au/Na Mordenite, the catalyst was found to deactivate by poisoning from a carbonate species. Only stable carbonates were observed on Au/Na-ZSM-5. The authors proposed a mechanism for Au/NaY, depicted in Scheme 94. [Pg.267]

Whilst today we can no longer accept either of these statements as literally and universally valid, they contain two very important and closely related ideas which have been proved useful. The first of these is that a normal, stable ester may become activated by interaction with another species a natural corollary of this is that esters can also be deactivated, or stabilised, by such interaction. The other idea is that in a series of esters gradations of polarity may be found, or that the polarity of any one ester, in particular the reactivity of the bond linking the potentially anionic and cationic moieties, may change according to the environment in which the ester finds itself. The two ideas are thus closely linked. One serious point in which I find myself in disagreement with Schmerling and Ipatieff and some contemporary writers is that, with respect to identifiable reaction intermediates,... [Pg.641]


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See also in sourсe #XX -- [ Pg.90 , Pg.91 , Pg.92 , Pg.93 ]




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Deactivation identifying activators

Identifying Activators and Deactivators

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