Departamento de Química, Laboratório de Química Computacional e Modelagem Molecular, ICEx, Universidade Federal de Minas Gerais, Campus Universitário, Pampulha, Belo Horizonte, Minas Gerais 31270-901, Brazil.
J Comput Chem. 2010 Jul 30;31(10):1986-2000. doi: 10.1002/jcc.21483.
DFT calculations were carried out to study the full catalytic cycle for the hydroformylation of propene, catalyzed by the heterobimetallic model catalyst trans-Pt(H)(PH(3))(2)(SnCl(3)). Before the study of the full catalytic cycle, the performance of six pure GGA, one GGA with inclusion of dispersion corrections, four hybrid-GGA, and three meta-GGA exchange correlation functional to describe a model reaction promoted by Pt-Sn catalyst were assessed. It is shown that the BP86 and GPW91 functionals, using extended basis set, provides reliable energetic results when compared with the CCSD(T) calculations. All intermediates and transition states along the elementary steps of the entire catalytic cycle were located and the energies involved in the catalytic cycle calculated using BP86 functional. The solvent effects along the entire catalytic cycle were evaluated using the polarizable continuum model. In contrast with the rhodium catalysts, the regioselectivity of the hydroformylation is set at the carbonylation step. The hydrogenolysis is the rate determining step of the entire cycle, with the activation energy of approximately 21 kcal mol(-1) in agreement with the experimental value of approximately 25 kcal mol(-1). The trans effect of the SnCl(3)(-) ligand seems to be pronounced only in the first step of the catalytic cycle, facilitating the insertion of the olefin into the Pt-H bond trans to it. The analysis of the stationary points obtained along each elementary step of the catalytic cycle is carried out separately and discussed. The BP86/cc-pVTZ/SBKJC results shows that the pathway leading to the linear aldehyde is preferred, being in agreement with the experimental findings.
采用密度泛函理论(DFT)计算研究了由异双核模型催化剂反式-Pt(H)(PH(3))(2)(SnCl(3))催化丙烯氢甲酰化的全催化循环。在研究全催化循环之前,评估了六种纯广义梯度近似(GGA)、一种包含色散校正的 GGA、四种混合广义梯度近似(hybrid-GGA)和三种泛函(meta-GGA)交换相关函数对 Pt-Sn 催化剂促进的模型反应的性能。结果表明,BP86 和 GPW91 泛函在使用扩展基组时,与 CCSD(T)计算相比,可以提供可靠的能量结果。利用 BP86 泛函,确定了整个催化循环中所有基元步骤的中间体和过渡态,并计算了催化循环中涉及的能量。使用极化连续体模型评估了整个催化循环中的溶剂效应。与铑催化剂不同,氢甲酰化的区域选择性在羰基化步骤中确定。氢解是整个循环的速率决定步骤,其活化能约为 21 kcal/mol,与约 25 kcal/mol 的实验值一致。SnCl(3)(-)配体的反式效应似乎仅在催化循环的第一步中明显,有利于烯烃插入与其反式的 Pt-H 键中。分别对催化循环的每个基元步骤中得到的稳定点进行了分析和讨论。BP86/cc-pVTZ/SBKJC 结果表明,线性醛的生成途径是有利的,与实验结果一致。