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Active sites, uniformity

Easy chemical manipulation of all catalytic sites is an important and widely recognized zeolite characteristic. The near uniformity of the intracrystalline surface (in the absence of protic sites) provides an excellent opportunity to treat active sites uniformly. With protic zeolites, the presence of extra-framework alumina and silica-alumina phases and the need to optimize interaction between protic and Lewis acid sites make chemical manipulation complex, particularly with aluminum-rich zeolites. [Pg.809]

The addition polymerization of a vinyl monomer CH2=CHX involves three distinctly different steps. First, the reactive center must be initiated by a suitable reaction to produce a free radical or an anion or cation reaction site. Next, this reactive entity adds consecutive monomer units to propagate the polymer chain. Finally, the active site is capped off, terminating the polymer formation. If one assumes that the polymer produced is truly a high molecular weight substance, the lack of uniformity at the two ends of the chain—arising in one case from the initiation, and in the other from the termination-can be neglected. Accordingly, the overall reaction can be written... [Pg.14]

As mentioned, corrosion is complexly affected by the material itself and the environment, producing various kinds of surface films, e.g., oxide or hydroxide film. In the above reactions, both active sites for anodic and cathodic reactions are uniformly distributed over the metal surface, so that corrosion proceeds homogeneously on the surface. On the other hand, if those reaction sites are localized at particular places, metal dissolution does not take place uniformly, but develops only at specialized places. This is called local corrosion, pitting corrosion through passive-film breakdown on a metal surface is a typical example. [Pg.218]

Figure 4.1. Representation of the pore structure of HZSM5, one of the most important zeolites industrially. The vertical cylinders represent one pore network, and the other cylinders an interconnecting network. The narrow pores, and their almost complete uniformity, means that only some molecules can enter. Others are excluded, and cannot react at the active sites, which are found within the structure. Thus, the reactivity of a molecule is determined by its shape and size, rather than by its electronic properties. Such a situation is almost unique, with the only exception being enzymes, where molecules must fit into the enzyme active site in order to react. Figure 4.1. Representation of the pore structure of HZSM5, one of the most important zeolites industrially. The vertical cylinders represent one pore network, and the other cylinders an interconnecting network. The narrow pores, and their almost complete uniformity, means that only some molecules can enter. Others are excluded, and cannot react at the active sites, which are found within the structure. Thus, the reactivity of a molecule is determined by its shape and size, rather than by its electronic properties. Such a situation is almost unique, with the only exception being enzymes, where molecules must fit into the enzyme active site in order to react.
The rate constants in table 4 for Ru/AlaOs should be considered as initial rate constants since it was not possible to achieve a higher coverage of N— than 0.25. Furthennorc, it was not possible to detect TPA peaks for Ru/AlaOs within the experimental detection limit of about 20 ppm. Ru/MgO is a heterogeneous system with respect to the adsorption and desorption of Na due to the presence of promoted active sites which dominate under NH3 synthesis conditions. The rate constant of desorption given in table 4 for Ru/MgO refers to the unpromoted sites [19]. The Na TPD, Na TPA and lER results thus demonstrate the enhancing influence of the alkali promoter on the rate of N3 dissociation and recombination as expected based on the principle of microscopic reversibility. Adding alkali renders the Ru metal surfaces more uniform towards the interaction with Na. [Pg.324]

However, we have to reflect on one of our model assumptions (Table 5.1). It is certainly not justified to assume a completely uniform oxide surface. The dissolution is favored at a few localized (active) sites where the reactions have lower activation energy. The overall reaction rate is the sum of the rates of the various types of sites. The reactions occurring at differently active sites are parallel reaction steps occurring at different rates (Table 5.1). In parallel reactions the fast reaction is rate determining. We can assume that the ratio (mol fraction, %a) of active sites to total (active plus less active) sites remains constant during the dissolution that is the active sites are continuously regenerated after AI(III) detachment and thus steady state conditions are maintained, i.e., a mean field rate law can generalize the dissolution rate. The reaction constant k in Eq. (5.9) includes %a, which is a function of the particular material used (see remark 4 in Table 5.1). In the activated complex theory the surface complex is the precursor of the activated complex (Fig. 5.4) and is in local equilibrium with it. The detachment corresponds to the desorption of the activated surface complex. [Pg.169]

Note 3 The location of active sites introduced into a polymer support depends on the type of polymer support. In a swollen-gel-bead polymer support the active sites are distributed uniformly throughout the beads, whereas in a macroporous-bead polymer support they are predominantly on the internal surfaces of the macropores. [Pg.248]

Deactivation may also be uniform for all sites, or it may be selective, in which case the more active sites, those which supply most of the catalyst activity, are preferentially attacked and deactivated. [Pg.473]


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