Neutral Catalyst Systems

A drawback to the use of commercial catalysts in ILs concerns the leaching of catalyst or catalyst residues into the organic solvents used for product isolation. This leads to high levels of product contamination, along with the rapid decrease of 

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In addition to simple asymmetric hydroacylation of alkenes, highly efficient desymmetrization of alkenes has also been achieved by Wu and co-workers. Interestingly, the catalyst system (Rh(I)-BINAP) differentiated the enantiotopic faces of the olefins and thus the cyclopentanone products were obtained with excellent ee s. The authors also showed that neutral and cationic Rh(I)-BINAP complexes furnished dififerent products. The neutral catalyst system preferentially fiunished the cw-3,4-disubstituted cyclopentanone, and the cationic catalyst afforded the trans isomer. 

I 5 Supported Catalysts and Nontraditional Reaction Media 5.3.2.1 Neutral Catalyst Systems... 

The proposed model [B] implies that syn selection in catalyzed hydroboration should decrease as the o-accepting character of the anti substituent decreases. This explains the higher syn selectivity in catalyzed hydroboration of allylic trifluoroacetates as compared with reactions of allylic acetates and carbamates [25]. The less diastereoselectivity of cationic complexes in hydroboration of chiral allylic systems than in the neutral catalyst systems [29, 30] is rationalized, as the latter have more electron density to shed via back-bonding. The anti selectivity in catalyzed hydroboration of the allylic acetate and trifluoroacetate is rationalized in terms of competition between the phenyl and acetate groups for the role of a acceptor. The further evidence is obtained in the case of pentafluo-... 

Montedison and Mitsui Petrochemical iatroduced MgCl2-supported high yield catalysts ia 1975 (7). These third-generation catalyst systems reduced the level of corrosive catalyst residues to the extent that neutralization or removal from the polymer was not required. Stereospecificity, however, was iasufficient to eliminate the requirement for removal of the atactic polymer fraction. These catalysts are used ia the Montedison high yield slurry process (Fig. 9), which demonstrates the process simplification achieved when the sections for polymer de-ashing and separation and purification of the hydrocarbon diluent and alcohol are eliminated (121). These catalysts have also been used ia retrofitted RexaH (El Paso) Hquid monomer processes, eliminating the de-ashing sections of the plant (Fig. 10) (129). 

High temperature acetylation of cellulose above 50°C produces cellulose acetate from low purity wood pulp cellulose in shorter reaction times. In a high temperature method recently disclosed (102), cellulose reacts with 200—400% acetic anhydride in the presence of <5% acid catalyst at 68—85°C for 3—20 min. After the acid catalyst is neutralized with magnesium acetate, the cellulose acetate is hydrolyzed at 120°C for two hours (103). Several modified catalyst systems have been developed for acetylation of cellulose above 90°C (89,90). 

In 1999, Kiindig and Bruin reported a closely related catalyst system 29a, in which a more readily accessible ligand has been employed [37]. Catalytic activity and stability are strongly dependent upon the nature of the neutral ligand L. While the acetonitrile complex 29b is stable, yet catalytically inactive, complex 29a with L = acrolein is stable only in the solid state, but decomposes as a solution in DCM... 

With reference to the homogeneous catalyst systems thus far reported for the synthesis of hydrocarbons/chemicals from carbon monoxide and hydrogen, only the anionic rhodium systems of Union Carbide show any appreciable shift activity. With neutral species of the type M3(CO)12 (M = Ru or Os), only small quantities of carbon dioxide are produced under the synthesis conditions (57). 

The first investigations of rhodium-catalyzed hydroformylation in room-temperature Hquid molten salts were published by Chauvin et al. in 1995 [6, 67]. The hydroformylation of 1-pentene with the neutral Rh(CO)2(acac)/triarylphosphine catalyst system was carried out as a biphasic reaction with [BMIM][Pp6] as the ionic liquid. 

Selectivity for each product formation may also be controlled by an effective catalyst system. After the discovery of the reaction by Heck, Stille applied the reaction to organic synthesis, as he observed the preferential formation of [3-methoxy esters under neutral conditions and 1,2-diesters in the presence of a base. As Bianchini reported in 2001, selective formation of a,/3-unsaturated ester product is established by an addition of protic acid such as y)-TsOH in bis-phosphine/Pd-catalyzed oxidative alkoxycarbonylation. ... 

The aromatic complex can be a neutral t °-benzene derivative or an anionic ri -cyclopentadienyl ring. Substituents on these aromatic rings can greatly influence the effectiveness of these catalysts. For example, with benzene derivatives the unsubstituted benzene rings give lower ees and the use of hexamethylbenzene results in lower catalytic activities whilst the cumenyl or mesityl rings give optimum catalyst systems. The two types of chiral bifunctional hnkers that have been most practical are anionic ones based on monosulfonated diamines and amino alcohols. 

PCH materials offer new opportunities for the rational design of heterogeneous catalyst systems, because the pore size distributions are in the supermicropore to small mesopore range (14-25A) and chemical functionality (e.g., acidity) can be introduced by adjusting the composition of the layered silicate host. The approach to designing PCH materials is based on the use of intercalated quaternary ammonium cations and neutral amines as co-surfactants to direct the interlamellar hydrolysis and condensation polymerization of neutral inorganic precursor (for example, tetraethylorthosilicate, TEOS) within the galleries of an ionic lamellar solid. 

Montedison and Mitsui Petrochemical introduced MgCl2-supported high yield catalysts in 1975, These third-generation catalyst systems reduced the level of corrosive catalyst residues to the extent that neutralization or... 

The generation of six-membered ring systems by means of cycloaddition reactions can be divided into two main approaches. The first is the cyclotrimerizationofalkynes utilizing low-valent iron catalyst systems, whereas the second approach is the Diels-Alder (DA) reaction of a diene and a dienophile. The latter reaction can itself be divided into three subclasses DA reactions with normal, neutral and inverse electron demand are known. The electronic structure of the educts dictates the oxidation state of the catalyst system required to perform the diverse classes of DA reactions. Nevertheless, for each subclass examples can be found. 

With the neutral [(RCN)2PdCl2] pro-catalyst system (Fig. 12.3, graph iv), computer simulation of the kinetic data acquired with various initial pro-catalyst concentrations and substrate concentrations resulted in the conclusion that the turnover rates are controlled by substrate-induced trickle feed catalyst generation, substrate concentration-dependent turnover and continuous catalyst termination. The active catalyst concentration is always low and, for a prolonged phase in the middle of the reaction, the net effect is to give rise to an apparent pseudo-zero-order kinetic profile. For both sets of data obtained with pro-catalysts of type B (Fig. 12.3), one could conceive that the kinetic product is 11, but (unlike with type A) the isomerisation to 12 is extremely rapid such that 11 does not accumulate appreciably. Of course, in this event, one needs to explain why the isomerisation of 11 now proceeds to give 12 rather than 13. With the [(phen)Pd(Me)(MeCN)]+ system, analysis of the relative concentrations of 11 and 13 as the conversion proceeds confirmed that the small amount of... 

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