Joseph Jorly, Rajanbabu T V, Jemmis Eluvathingal D
School of Chemistry, University of Hyderabad, Central University P. O., Hyderabad 500046, India, Department of Inorganic and Physical Chemistry, Indian Institute of Science, Bangalore 560012, India, Indian Institute of Science Education and Research, Thiruvananthapuram, CET Campus, Kerala 695016, India, and Department of Chemistry, The Ohio State University, 100 W. 18th Avenue, Columbus, Ohio 43210.
Organometallics. 2009 Jun 22;28(12):3552-3566. doi: 10.1021/om900045p.
We report a detailed and full computational investigation on the hydrovinylation reaction of styrene with the Ni(II)-phospholane catalytic system, which was originally presumed to proceed through a cationic mechanism involving a nickel hydride intermediate. The following general features emerge from this study on a specific catalyst complex that was found to give quantitative yield and moderate selectivity: (a) the activation barrier for the initiation (18.8 kcal/mol) is higher than that for the reaction due to a low-lying square-planar pentenyl chelate intermediate originating from a Ni(II)-allyl catalyst precursor. Consequently there is an induction period for the catalysis; (b) the exit of product from the catalyst is via a β-H-transfer step instead of the usual β-H elimination pathway, which has a very high activation energy due to a trans effect of the phospholane ligand; (c) the turnover-limiting and enantio- determining transition state is also the β-H-transfer; (d) because of the absence of a hydride intermediate, the unwanted isomerization of the product is prevented; (e) since the enantio-discrimination is decided at the H-transfer stage itself, the configuration of the product in a catalytic cycle influences the enantioselectivity in the subsequent cycle; (f) the trans effect of the sole strong ligand in the d8 square-planar Ni(II), the stability of the η(3)-benzyl intermediate, and the availability of three coordination sites enable regioselective hydrovinylation over the possible oligomerization/polymerization of the olefin substrates and linear hydrovinylation. This work has also confirmed the previously recognized role of the hemilabile group at various stages in the mechanism.
我们报道了对苯乙烯与Ni(II)-膦烷催化体系的氢乙烯基化反应进行的详细且全面的计算研究,该反应最初被认为是通过涉及氢化镍中间体的阳离子机理进行的。对一种特定催化剂配合物的研究得出了以下一般特征,该配合物被发现能给出定量产率和适度选择性:(a)引发的活化能垒(18.8 kcal/mol)高于反应的活化能垒,这是由于源自Ni(II)-烯丙基催化剂前体的低平面戊烯基螯合物中间体所致。因此催化存在诱导期;(b)产物从催化剂上的离去是通过β-H转移步骤,而不是通常的β-H消除途径,由于膦烷配体的反位效应,β-H消除途径具有非常高的活化能;(c)周转限制和对映体决定的过渡态也是β-H转移;(d)由于不存在氢化中间体,防止了产物不想要的异构化;(e)由于对映体区分在H转移阶段本身就已决定,催化循环中产物的构型会影响后续循环中的对映选择性;(f)d8平面正方形Ni(II)中唯一强配体的反位效应、η(3)-苄基中间体的稳定性以及三个配位位点的可用性使得在烯烃底物可能的低聚/聚合和线性氢乙烯基化反应中实现区域选择性氢乙烯基化。这项工作也证实了先前认识到的半不稳定基团在该机理各个阶段的作用。