Selectivity increase

Multiple reactions. For multiple reactions in which the byproduct is formed in parallel, the selectivity may increase or decrease as conversion increases. If the byproduct reaction is a higher order than the primary reaction, selectivity increases for increasing reactor conversion. In this case, the same initial setting as single reactions should be used. If the byproduct reaction of the parallel system is a... 

Use of HRh(CO)[P(CgH )2]3 as the catalyst and an excess of triphenylphosphine improves the y P ratio. For example, reaction of triethoxysilane with allylamine of equivalent moles at 150°C for 10 h, yields the y-form product ia more than 70% and the y P ratio is 26. Compared with this, when H2PtCl3 is used as the catalyst, the y P ratio is 4 (41). Furthermore, when Rh[(p.-P(C3H3)2-(cyclooctadiene)]2 is used as the catalyst, the yield of y-form product is selectively increased to 92% and that of P-form product is decreased to 1.1% (42). 

In addition to the boron trifluoride-diethyl ether complex, chlorotrimcthylsilanc also shows a rate accelerating effect on cuprate addition reactions this effect emerges only if tetrahydrofuran is used as the reaction solvent. No significant difference in rate and diastereoselectivity is observed in diethyl ether as reaction solvent when addition of the cuprate, prepared from butyllithium and copper(I) bromide-dimethylsulfide complex, is performed in the presence or absence of chlorotrimethylsilane17. If, however, the reaction is performed in tetrahydrofuran, the reaction rate is accelerated in the presence of chlorotrimethylsilane and the diastereofacial selectivity increases to a ratio of 88 12 17. In contrast to the reaction in diethyl ether, the O-silylated product is predominantly formed in tetrahydrofuran. The alcohol product is only formed to a low extent and showed a diastereomeric ratio of 55 45, which is similar to the result obtained in the absence of chlorotrimethylsilane. This discrepancy indicates that the selective pathway leading to the O-silylated product is totally different and several times faster than the unselective pathway" which leads to the unsilylated alcohol adduct. A slight further increase in the Cram selectivity was achieved when 18-crown-6 was used in order to increase the steric bulk of the reagent. 

Addition of 15-crown-5 to the higher-order cuprate led to a reagent that is totally unrcac-tive towards 2-phenylpropanal even at room temperature18. If, however, boron trifluoride-diethyl ether complex was added as additional ingredient, the reactivity was restored and, furthermore, the Cram selectivity increased to 90 10 (Table 4). Analogous results could be obtained by placing the crown-ether effect within the cuprate itself, as in reagent 10. 

The diastereomeric excess (d.e.) of 76a reached 72% (epoxidation) and 98% (dihydroxylation). Nitro substitution on the aromatic ring (as in 77a) significantly reduced the selectivity (increased the syn proportion), although anti preference was stiU retained in epoxidation (20% d.e.) and in dihydroxylation (68% d.e.). 

The reactivity and product selectivity increase as dispersing agents were introduced. Simultaneously, a higher silicon conversion was also obtained. A higher silicon conversion will decrease the burden of waste disposal. Therefore, this study provides a convenient and economical way for the preparation of highly effective CuCl catalyst that can be used in practical production using the direct process. 

In the synthesis of DMC fiom the transesterification of EC and methanol, quaternary ammonium salt catalysts showed good catalytic activity. The main byproduct was ethylene glycol. The quaternary salt with the cation of bulkier alkyl chain laigth and witii more nucleophilic anion showed better reactivity. Hi temperature and large amount of catalyst increased the conversion of EC. The EC conversion and DMC selectivity increased as the pressure of CO2 increased from 250 to 350 psig. 

For small particles, selectivity increases with particle size (14,30) In our results, Ag(lll) has an average selectivity which is about 6% higher (in absolute units) than Ag(llO) (28). Since the particle surface should evolve from open, or (110)-like, to close-packed, or (lll)-like, with increasing size, these results may be favorably correlated. 

One feature of Fig. 5 is overwhelmingly obvious. Any changes in the kinetic parameters (E, m,n) for EtO production are mimicked almost exactly by those for 6O2 production. Thus there is nothing in Fig. 5 which helps to explain the very large selectivity increase... 

The selectivity changes in a more complex way For K -, Ca - and B -modified alumina no change in selectivity is observed. In the case when Li cation is added to y-alumina, Aj product selectivity increases to 0.4 from 0.26 for pure y-Al205. The highest selectivity of Aj product (0.62) is observed for Mg -modified alumina. 

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