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Para-selectivity requirements

Rigorous treatment of the para-selectivity requires a knowledge of the intrinsic value of the rate constant for all the reactions involved and of the absolute value of the crystal size and of the diffusivity, all under reaction conditions. These values are obtainable only with considerable difficulty and effort. As has been mentioned, the 30 percent sorption time for o-xylene at 120°c, t0.3/ is proportional to the actual values, r2/D. [Pg.296]

As is apparent from the previous discussion on toluene disproportionation,the observation of high p-selectivity in STDP requires a dramatic change in selectivity. First, the primary product must be directed to be highly para-selective. Secondly, the subsequent isomerization of the primary p-xylene product must be selectively inhibited ... [Pg.283]

Some zeolitic and non-zeolitic molecular sieve catalysts are claimed to be capable for ortho- and para-selective alkylation using olefin as alkylating agent (refs. 1,2). Zeolite catalysts are less active and selective in the methylation of aniline by methanol (refs. 3,4). Reaction is usually carried out with a large excess of methanol since a large fraction of the alcohol decomposes without participating in the alkylation. Numerous N- and C-alkylated aniline derivatives appear in the reaction product. It was found that N-alkylation requires basic sites while C-alkylation occurs mainly on acidic sites (refs. 5-7). [Pg.523]

Nitration of monosubstituted aromatics, toluene in particular, has been extensively studied using zeolites in order to direct the reaction towards the formation of the desired para-isomer. Toluene has been nitrated para-selectively with benzoyl nitrate over zeolite catalysts.[14,15] For example, when mordenite is used as a catalyst, MNTs are formed in almost quantitative yields, giving 67 % of the para-isomer in 10 min, but tetrachloromethane is required as solvent. However, the main problems associated with the use of benzoyl nitrate are handling difficulties due to its sensitivity toward decomposition, and the tendency toward detonation upon contact with rough surfaces. Nagy et a/.[19 21] reported the nitration of benzene, chlorobenzene, toluene and o-xylene with benzoyl nitrate in the presence of an amorphous aluminosilicate, as well as with zeolites HY and ZSM-11, in hexane as a... [Pg.107]

We have reported the use of zeolite HP in conjunction with a mixture of acetic anhydride and nitric acid, which currently offers the best combination of yield and para-selectivity for nitration of simple aromatic compounds.11 For example, this system allows quantitative mononitration of toluene with selectivity for the para isomer of around 80 %. For commercial production of 4-nitrotoluene this would require less than half the toluene or nitric acid needed for the conventional mixed acid method and would generate less than one third of the waste. In general, the system offers excellent possibilities for nitration of substrates of moderate activity. However, it is not very successful with deactivated substrates. One aspect of the work reported here is therefore the modification of this approach so that it accommodates deactivated substrates. [Pg.234]

Continued low-level addition of heterocycle was required to maintain para-selectivity. In an example case at 404 C, using an alumina-binder containing catalyst, about 15 ppm N (as o-pbenanthroline) was required to maintain %-97% para-selectivity. Less is required at lower temperature less is required with binder-free catalyst. [Pg.618]

This Safety Guide is intended to have general applicability to any type of research reactor. However, the particular characteristics of research reactors, as mentioned in para. 102, require some flexibility in the fulfilment of the requirements and the application of the guidelines given in this Safety Guide. Therefore, it is necessary that users of this Safety Guide make a conscious and justifiable selection of the information offered. In addition, the extent of detail in the application of the... [Pg.2]

With toluene as substrate formylation proceeded in a high yield (99%) with respect to aldehyde formation and with good para-selectivity (90%) in a reaction time of only 1 hour. The reaction was carried out on phenol under the same reaction conditions. Surprisingly, the reactivity of phenol proved to be much lower than that of toluene and a reaction time of more than 4 hours was required to obtain acceptable yields, albeit with reduced para-selectivity. When the reaction was extended to anisole, only small differences compared to phenol were observed within the first hour of the reaction, but at extended reaction times phenol proved to give better conversions. The results indicate that the reaction is sustained for a longer time with phenol than with anisole. [Pg.43]

These three steps all produce significant amounts of waste. First, as discussed earlier, the nitration process results in the production of spent sulfuric acid. In the past the company had been able to sell much of this material to the coke and steel industries but declining demand meant that the acid now required disposing of, at additional cost. At the time green catalytic nitration technology was becoming available with clay, zeolite and lanthanide catalysts all providing possible alternatives to the use of sulfuric acid (see below). Improved selectivity to the desired para-isomer is an added benefit of some of these catalytic systems. However on the... [Pg.260]

Aryl halides can also be reduced by tin hydrides76,77, although these reactions always require initiators because the stronger C—X bonds in aryl halides are less reactive than the C—X bonds in alkyl halides. In fact, a series of meta- and para-substituted bromobenzenes, where X is either meta- or para-CH3O-, C=N, Cl, F, CF3, CH3, Bu-f or 2,6-dichloro, have been reduced by tributyltin deuteride (equation 60). It is worth noting that the more reactive bromide is reduced selectively in the presence of the less reactive chloride and fluoride groups (equation 61). [Pg.788]

The first report to use diphosphite ligands in the asymmetric hydroformylation of vinyl arenes revealed no asymmetric induction [46]. An important breakthrough came in 1992 when Babin and Whiteker at Union Carbide patented the asymmetric hydroformylation of various alkenes with ee s up to 90%, using bulky diphosphites 2a-c derived from homochiral (2R, 4R)-pentane-2,4-diol (Scheme 4) [17]. Their early results showed that (a) bulky substituents are required at the ortho positions of the biphenyl moieties for good regio- and enantio-selectivity and (b) methoxy substituents in the para positions of the biphenyl moieties always produced better enantio-selectivities than those observed for the corresponding ferf-butyl-substituted analogues. [Pg.51]

One may formulate in general terms a complementarity of rules for thermal and photochemical processes. However, such a generalization could possibly predict ortho-para orientation but not activation. First of all, careful experimental testing of the hypothesis seems required. We present a selection of very recent results. ... [Pg.247]


See other pages where Para-selectivity requirements is mentioned: [Pg.697]    [Pg.105]    [Pg.11]    [Pg.3]    [Pg.287]    [Pg.492]    [Pg.267]    [Pg.267]    [Pg.106]    [Pg.112]    [Pg.541]    [Pg.236]    [Pg.3323]    [Pg.267]    [Pg.342]    [Pg.665]    [Pg.530]    [Pg.281]    [Pg.3322]    [Pg.186]    [Pg.615]    [Pg.105]    [Pg.3]    [Pg.17]    [Pg.489]    [Pg.444]    [Pg.325]    [Pg.172]    [Pg.884]    [Pg.351]    [Pg.106]    [Pg.106]    [Pg.166]    [Pg.500]    [Pg.515]    [Pg.118]    [Pg.313]   


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Para-selectivity

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