Inhibition, catalysts

Fig. 6. Catalyst inhibition mechanisms where ( ) are active catalyst sites the catalyst carrier and the catalytic support (a) masking of catalyst (b) poisoning of catalyst (c) thermal aging of catalyst and (d) attrition of ceramic oxide metal substrate monolith system, which causes the loss of active catalytic material resulting in less catalyst in the reactor unit and eventual loss in performance.

A short and efficient synthetic approach to hydroxy-substituted ( )-stil-benoids, as exemplified by the natural compound resveratrol (371b) via solid-phase CM, was reported by a Korean group (Scheme 71) [154]. When two different stilbenes were allowed to couple by catalyst C, all three kinds of possible stilbenes were obtained as an inseparable mixture. Anchoring 4-vinylphenol to Merrifield resin, followed by exposing the supported styrenyl ether 368 and diacetoxy styrene 369 (10 equiv) to the catalyst, inhibited self-metathesis of the supported substrate. Sequential separation of the homodimer formed from 369 by washing and subsequent cleavage of the resin 370 with acid provided (E)-stilbene 371a with complete stereocontrol in 61% yield. 

The stability of catalyst is one of the most important criteria to evaluate its quality. The influence of time on stream on the conversion of n-heptane at SSO C is shown in Fig. 5. The conversion of n-heptane decreases faster on HYl than on FIYs with time, so the question is Could the formation of coke on the catalyst inhibit diffusion of reactant into the caves and pores of zeolite and decrease the conversion According to Hollander [8], coke was mainly formed at the beginning of the reaction, and the reaction time did not affect the yield of coke. Hence, this decrease might be caused by some impurities introduced during the catalyst synthesis. These impurities could be sintered and cover active sites to make the conversion of n-heptane on HYl decrease faster. 

Vedejs et al. reported catalyst inhibition during a study on the enantioselective transfer hydrogenation of dihydro-isoquinolines using Noyori s catalyst (Scheme 44.2) [27]. Here, the problem is caused by the bidentate nature of the substrate. Whereas the bromo compound 1 a could be rapidly reduced, the tosylamide-sub-stituted compound lb could not be reduced, and although the problem could be alleviated somewhat by alkylation of the sulfmamide to 1 c, hydrogenation of this was still sluggish. Although the authors propose this to be a case of product... 

Scheme 44.2 Catalyst inhibition caused by functional groups in the substrate.

Scheme 44.5 Catalyst inhibition through formation of stable arene complex.

Catalyst Inhibition Caused by Compounds Containing Heteroatoms... 

Dyson recently warned that chloride impurities present in ionic liquids prepared by the classical metathesis reaction may cause severe catalyst inhibition. This may be aggravated by the fact that metal-chloride dissociation is disfavored in ionic liquids, in spite of their polar nature [77]. 

To date, the best studied modified systems are Pt catalysts inhibited with sulfur compounds, morpholine or phosphorous compounds (ref. 5). Raney nickel modified with dicyandiamide has also been reported to be able to hydrogenate aromatic chloronitro compounds with very good selectivities and activities. Since nickel is an attractive alternative to precious metal catalysts we decided to search for other types of inhibitors and to investigate the stage at which dehaiogenation occurs. 

Catalyst Inhibition. A number of potential applications for catalytic oxidation of organic materials have resulted in serious odor or eye... 

The kinetics of alkylation by benzyl bromide of the Schiff base esters of ammo acids (Ph2C=NCH2CC>2CMe3) in the presence of cinchona salts show features similar to those of enzyme-promoted reactions variable orders, substrate saturation, catalyst inhibition, and non-linear Arrhenius-type plots.125 A tight coordination of the Schiff base substrate by electrostatic interaction with the quaternary N of the cinchona salt provides a favourable chiral environment for asymmetric alkylation. 

In spite of all of the work, the kinetics and mechanism of alkyl-substituted dibenzothiophene, where the sulfur atom may be sterically hindered, are not well understood and these compounds are in general very refractory to hydrodesulfurization. Other factors that influence the desulfurization process such as catalyst inhibition or deactivation by hydrogen sulfide, the effect of nitrogen compounds, and the effect of various solvents need to be studied in order to obtain a comprehensive model that is independent of the type of model compound or feedstock used. 

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