Di Tommaso Devis, French Samuel A, Zanotti-Gerosa Antonio, Hancock Fred, Palin Erika J, Catlow C Richard A
Davy Faraday Research Laboratory, Kathleen Lonsdale Building, University College of London, Gower Street, London WC1E 6BT, United Kingdom.
Inorg Chem. 2008 Apr 7;47(7):2674-87. doi: 10.1021/ic701981v. Epub 2008 Mar 5.
The reduction of prochiral ketones catalyzed by Ru(diphosphine)(diamine) complexes has been studied at the DFT-PBE level of theory. Calculations have been conducted on real size systems [trans-Ru(H)2(S, S-dpen)(S-xylbinap) + acetophenone], [trans-Ru(H)2(S, S-dpen)(S-tolbinap) + acetophenone] and [trans-Ru(H)2(S, S-dpen)(S-xylbinap) + cyclohexyl methyl ketone] with the aim of identifying the factors controlling the enantioselectivity in Ru(diphosphine)(diamine) catalysts. The high enantiomeric excess (99%) in the hydrogenation of acetophenone catalyzed by trans-Ru(H)2(S, S-dpen)(S-xylbinap) has been explained in terms of the existence of a stable intermediate along the reaction pathway associated with the (R)-alcohol. The formation of this intermediate is hindered with the competitive pathways, which consequently increases the activation energy for the hydrogen transfer acetophenone/(S)-phenylethanol reaction. For the [trans-Ru(H)2(S, S-dpen)(S-tolbinap) + acetophenone] system, the lower enantioselectivity (i.e. 80%) is rationalized by the smaller differences in the activation energy between the competitive pathways which differentiate between the two diastereomeric approaches of the prochiral ketone. The DFT-PBE results suggest that this reaction is driven to the (R)-product only by the process of binding the acetophenone to the active site of the trans-Ru(H) 2(S, S-dpen)(S-tolbinap) catalyst. For the hydrogenation of cyclohexyl methyl ketone catalyzed by trans-Ru(H)2(S, S-dpen)(S-xylbinap), the low performance in the enantioselective hydrogenation of the dialkyl ketone (i.e. 37%) is again explained by the small differences in the activation and binding energies which are the factors which could effectively differentiate between the two alkyl groups.
已在DFT-PBE理论水平上研究了Ru(二膦)(二胺)配合物催化前手性酮的还原反应。对实际尺寸的体系[反式-Ru(H)₂(S,S-二苯乙二胺)(S-联萘酚二甲苯) + 苯乙酮]、[反式-Ru(H)₂(S,S-二苯乙二胺)(S-联萘酚甲苯) + 苯乙酮]和[反式-Ru(H)₂(S,S-二苯乙二胺)(S-联萘酚二甲苯) + 环己基甲基酮]进行了计算,目的是确定控制Ru(二膦)(二胺)催化剂对映选择性的因素。反式-Ru(H)₂(S,S-二苯乙二胺)(S-联萘酚二甲苯)催化苯乙酮氢化反应中高对映体过量(99%)的现象,已根据反应途径中与(R)-醇相关的稳定中间体的存在来解释。该中间体的形成受到竞争途径的阻碍,这相应地增加了苯乙酮/(S)-苯乙醇氢转移反应的活化能。对于[反式-Ru(H)₂(S,S-二苯乙二胺)(S-联萘酚甲苯) + 苯乙酮]体系,较低的对映选择性(即80%)可通过前手性酮两种非对映体方法之间竞争途径的活化能差异较小来解释。DFT-PBE结果表明,该反应仅通过苯乙酮与反式-Ru(H)₂(S,S-二苯乙二胺)(S-联萘酚甲苯)催化剂活性位点的结合过程而生成(R)-产物。对于反式-Ru(H)₂(S,S-二苯乙二胺)(S-联萘酚二甲苯)催化的环己基甲基酮氢化反应,二烷基酮对映选择性氢化反应的低性能(即37%)同样可通过活化能和结合能差异较小来解释,这些能量差异是能够有效区分两个烷基的因素。