Department of Chemistry, Chemistry Research Laboratories , University of Oxford , Mansfield Road , Oxford OX1 4TA , U.K.
Early Chemical Development , Pharmaceutical Sciences, IMED Biotech Unit, AstraZeneca , Macclesfield SK10 2NA , U.K.
J Am Chem Soc. 2018 Jun 13;140(23):7347-7357. doi: 10.1021/jacs.8b04086. Epub 2018 May 29.
The detailed mechanism of the hydroacylation of β-amido-aldehyde, 2,2-dimethyl-3-morpholino-3-oxopropanal, with 1-octyne using [Rh( cis-κ--DPEPhos)(acetone)][BAr]-based catalysts, is described [Ar = (CF)CH]. A rich mechanistic landscape of competing and interconnected hydroacylation and cyclotrimerization processes is revealed. An acyl-hydride complex, arising from oxidative addition of aldehyde, is the persistent resting state during hydroacylation, and quaternary substitution at the β-amido-aldehyde strongly disfavors decarbonylation. Initial rate, KIE, and labeling studies suggest that the migratory insertion is turnover-limiting as well as selectivity determining for linear/branched products. When the concentration of free aldehyde approaches zero at the later stages of catalysis alkyne cyclotrimerization becomes competitive, to form trisubstituted hexylarenes. At this point, the remaining acyl-hydride turns over in hydroacylation and the free alkyne is now effectively in excess, and the resting state moves to a metallacyclopentadiene and eventually to a dormant α-pyran-bound catalyst complex. Cyclotrimerization thus only becomes competitive when there is no aldehyde present in solution, and as aldehyde binds so strongly to form acyl-hydride when this happens will directly correlate to catalyst loading: with low loadings allowing for free aldehyde to be present for longer, and thus higher selectivites to be obtained. Reducing the catalyst loading from 20 mol % to 0.5 mol % thus leads to a selectivity increase from 96% to ∼100%. An optimized hydroacylation reaction is described that delivers gram scale of product, at essentially quantitative levels, using no excess of either reagent, at very low catalyst loadings, using minimal solvent, with virtually no workup.
详细描述了[Rh(顺式-κ-DPEPhos)(丙酮)][BAr] - 基催化剂用于β-酰胺基醛,2,2-二甲基-3-吗啉-3-氧代丙醛与 1-辛炔的水合酰化反应的机理[Ar =(CF 3)CH]。揭示了竞争和相互关联的水合酰化和环三聚化过程的丰富机理景观。醛的氧化加成产生的酰基氢化物复合物是水合酰化过程中的持久静止状态,β-酰胺基醛的季铵取代强烈不利于脱羰。初始速率、KIE 和标记研究表明,迁移插入既是限速步骤,也是线性/支化产物的选择性决定因素。当催化后期游离醛的浓度接近零时,炔烃环三聚化变得具有竞争力,形成三取代己基芳烃。此时,剩余的酰基氢化物在水合酰化中转化,游离的炔烃现在实际上过量,并且静止状态移动到金属环戊二烯并最终移动到休眠的α-吡喃结合催化剂络合物。因此,只有当溶液中没有醛存在时,环三聚化才具有竞争力,并且当醛强烈结合形成酰基氢化物时,与催化剂负载量直接相关:负载量越低,允许更长时间存在游离醛,从而获得更高的选择性。将催化剂负载量从 20 mol%降低至 0.5 mol%,从而使选择性从 96%提高到约 100%。描述了一种优化的水合酰化反应,该反应使用非常低的催化剂负载量、最小的溶剂用量,在没有过量试剂的情况下,从实质上定量的水平提供克级产品,几乎无需后处理。