Second-generation catalysts

RCM of MBH adducts 144 by Grubbs catalyst (second generation) furnished cyclized products that underwent elimination of water to afford cyano-naphthalenes 145 in excellent yields (Scheme 4.41). 

Grubbs catalyst second-generation XXVin was used in 2009 by Botta and coworkers in a multicomponent procedure for the preparation of 2,3-dihydropyrans (Section 5.3.2.2, Scheme 5.57). As an application of this MCR, furanose-pyranose C—C-linked disaccharide 106 was obtained as a mixture of four diastereoisomers, which after equihbration with ZnClj and hydrogenation afford 107a,b (Scheme 5.80). This reaction constitutes a versatile and effective approach for the preparation of biologically interesting building blocks in carbohydrate chemistry [80]. 

Grubbs catalyst second generation permanently coated capillary... 

First generation Grubbs catalyst Second generation Grubbs catalyst (commercially available) (commercially available)... 

TiCl catalysts produced by the reduction of TiCl with Al(C2H 2d> subsequentiy treated first with an electron donor (diisoamyl ether), then with TiCl, are highly stereospecific and four to five times more active than d-TiCl (6). These catalysts were a significant advance over the earlier TiCl systems, because removal of atactic polymer was no longer required. They are often referred to as second-generation catalysts. The life of many older slurry process faciUties has been extended by using these catalysts to produce "clean" polymers with very low catalyst residues. 

These catalysts contained promoters to minimise SO2 oxidation. Second-generation systems are based on a combined oxidation catalyst and particulate trap to remove HC and CO, and to alleviate particulate emissions on a continuous basis. The next phase will be the development of advanced catalysts for NO removal under oxidising conditions. Low or 2ero sulfur diesel fuel will be an advantage in overall system development. 

To overcome these problems with the first generation Brmsted acid-assisted chiral Lewis acid 7, Yamamoto and coworkers developed in 1996 a second-generation catalyst 8 containing the 3,5-bis-(trifluoromethyl)phenylboronic acid moiety [10b,d] (Scheme 1.15, 1.16, Table 1.4, 1.5). The catalyst was prepared from a chiral triol containing a chiral binaphthol moiety and 3,5-bis-(trifluoromethyl)phenylboronic acid, with removal of water. This is a practical Diels-Alder catalyst, effective in catalyzing the reaction not only of a-substituted a,/ -unsaturated aldehydes, but also of a-unsubstituted a,/ -unsaturated aldehydes. In each reaction, the adducts were formed in high yields and with excellent enantioselectivity. It also promotes the reaction with less reactive dienophiles such as crotonaldehyde. Less reactive dienes such as isoprene and cyclohexadiene can, moreover, also be successfully employed in reactions with bromoacrolein, methacrolein, and acrolein dienophiles. The chiral ligand was readily recovered (>90%). 

The LLB catalysts requires at least 3.3 mol% of asymmehic catalyst for efficient nitro-aldol reactions, and the reactions are rather slow (first generation). Second-generation LLB catalysts are prepared by addition of 1 equiv of H2O and 0.9 equiv of n-BuLi. The second-generation-catalysts are more reactive than the first generation LLB as shown in Eq. 3.80. The proposed mechanism of asymmetiic niti o-aldol reaction using these catalysts is presented in Scheme 3.20. ... 

The chapter by Blum et al. covers another candidate second-generation process. This approach uses a large circulating catalyst-liquid slurry stream as the thermal flywheel to control the temperature rise. This is analogous to the H-Oil proces used for hydrotreating oil (2). 

Origins of Enhanced Reactivity of Second-Generation Metathesis Catalysts 244... 

The mechanistic investigations presented in this section have stimulated research directed to the development of advanced ruthenium precatalysts for olefin metathesis. It was pointed out by Grubbs et al. that the utility of a catalyst is determined by the ratio of catalysis to the rate of decomposition [31]. The decomposition of ruthenium methylidene complexes, which attribute to approximately 95% of the turnover, proceeds monomolecularly, which explains the commonly observed problem that slowly reacting substrates require high catalyst loadings [31]. This problem has been addressed by the development of a novel class of ruthenium precatalysts, the so-called second-generation catalysts. 

The cross metathesis of acrylic amides [71] and the self metathesis of two-electron-deficient alkenes [72] is possible using the precatalyst 56d. The performance of the three second-generation catalysts 56c,d (Table 3) and 71a (Scheme 16) in a domino RCM/CM of enynes and acrylates was recently compared by Grimaud et al. [73]. Enyne metathesis of 81 in the presence of methyl acrylate gives the desired product 82 only with phosphine-free 71a as a pre-... 

The metathesis of ene-ynamides has been investigated by Mori et al. and Hsung et al. [80]. Second-generation ruthenium catalysts and elevated temperatures were required to obtain preparatively useful yields. Witulski et al. published a highly regioselective cyclotrimerization of 1,6-diynes such as 98 and terminal alkynes using the first-generation ruthenium metathesis catalyst 9... 

Few reports describe the cross metathesis of allyl halides [88]. First-generation catalyst 9 does not seem to be sufficiently reactive to promote this reaction in preparatively useful yields and acceptable catalyst loadings, but second-generation catalyst 56d gives good results for allyl chloride. Cross-metathesis... 

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