首页> 外文期刊>Journal of the Chemical Society, Dalton Transactions. Inorganic Chemistry >Mechanistic aspects of hydrogen addition during enantioselective rhodium-catalysed reductio of C=C double bonds with formic acid/triethylamine or molecular hydrogen
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Mechanistic aspects of hydrogen addition during enantioselective rhodium-catalysed reductio of C=C double bonds with formic acid/triethylamine or molecular hydrogen

机译:甲酸/三乙胺或分子氢对映体选择性铑催化的C = C双键还原过程中加氢的机理

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摘要

Deuterium labelling experiments reveal a remarkably different hydrogen addition mode during homogeneously catalysed C=C bond reduction of itaconic acid derivatives 1a-d using molecular hydrogen atoms across the double bond prevails for all substrates in conventional hydrogenation, whereas the deuterium pattern depends largely on the nature of the carboxyl group in the beta (or allylic) position during transfer hydrogenation. Vicinal addition is observed only in case of itaconic acid 1a and alpha-methylitaconate 1c, while 1,3-addition is preferred with dimethylitaconate 1b and beta-methylitaconate 1d. Significant amounts of polydeuterated products are formed also during hydrogenation and transfer hydrogenation. Monitoring the deuterium pattern as a function of time reveals that deuterium scrambling is responsible for polydeuteration, but not for the change of the change of the addition mode. The use of monodeuterted formic acid isotopomers shows that the incorporation from the hydridic formyl position occurs preferentially at the terminal end of the double bond (C-3) whereas the protic hydrogen is directed either in the higher substituted olefinic (C-2) or the methylene (C-1) position. Control experiments using mesaconic (2) and citraconic (30 acids demonstrate that double bond migration in 1a-d is negligible under the reaction conditions. These results are best rationalised on the basis of a common mechanism for hydrogenation and transfer hydrogenation that involves (i) the generation of Rh-H intermediates, (ii) reversible hydride transfer to coordinated substrate to form two isomeric sigma-alkyl intermediates, and (iii) irreversible product liberation through protolytic Rh-C cleavage. The key intermediates are similar if not identical for hydrogenation and transfer hydrogenation. The change of the hydrogen transfer pattern can be explained on the basis of the relative rates of the individual steps within the catalytic cycle as compared to the rate of isomerisation of the sigma-alkyl intermediates.
机译:氘标记实验显示,在传统氢化中,所有底物上均使用跨双键的分子氢原子,在衣康酸衍生物1a-d均相催化的C = C键还原过程中,氢的加成方式显着不同,而氘的模式主要取决于性质转移氢化过程中β(或烯丙基)位置的羧基的摩尔数仅在衣康酸1a和α-甲基衣康酸酯1c的情况下才观察到邻位添加,而优选将1,3-添加与衣康酸二甲酯1b和β-甲基衣康酸酯1d一起使用。在氢化和转移氢化期间也形成大量的多氘代产物。监测氘随时间的变化规律表明,氘加扰是多氘化的原因,而不是加成模式变化的变化。单氘代甲酸异位异构体的使用表明,从氢化甲酰基位置开始的掺入优先发生在双键(C-3)的末端,而质子氢则直接在较高取代的烯烃(C-2)或亚甲基(C-1)位置。使用中松香(2)和柠康酸(30种酸)的对照实验表明,在反应条件下,1a-d中的双键迁移可忽略不计,这些结果最好根据涉及以下条件的加氢和转移加氢的通用机理来合理化: Rh-H中间体的产生;(ii)可逆的氢化物转移到配位的底物上,形成两个异构的sigma-烷基中间体;(iii)通过水解性的Rh-C裂解产生不可逆的产物。氢转移模式的变化可以基于与σ-烷基中间体的异构化速率相比在催化循环内各个步骤的相对速率来解释。

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