School of Chemical & Biomolecular Engineering, Georgia Institute of Technology, 311 Ferst Dr, Atlanta, GA, 30332, USA.
Department of Chemistry, Emory University, 1515 Dickey Drive, Atlanta, GA, 30322, USA.
Angew Chem Int Ed Engl. 2020 Oct 26;59(44):19525-19531. doi: 10.1002/anie.202005381. Epub 2020 Jul 8.
Herein we demonstrate a packed bed flow reactor capable of achieving highly regio- and stereoselective C-H functionalization reactions using a newly developed Rh (S-2-Cl-5-CF TPCP) catalyst. To optimize the immobilized dirhodium catalyst employed in the flow reactor, we systematically study both (i) the effects of ligand immobilization position, demonstrating the critical factor that the catalyst-support attachment location can have on the catalyst performance, and (ii) silica support mesopore length, demonstrating that decreasing diffusional limitations leads to increased accessibility of the active site and higher catalyst turnover frequency. We employ the immobilized dirhodium catalyst in a simple packed bed flow reactor achieving comparable yields and levels of enantioselectivity to the homogeneous catalyst employed in batch and maintain this performance over ten catalyst recycles.
在此,我们展示了一种填充床流动反应器,使用新开发的 Rh(S-2-Cl-5-CF TPCP)催化剂,能够实现高度区域和立体选择性的 C-H 功能化反应。为了优化用于流动反应器的固定化双铑催化剂,我们系统地研究了(i)配体固定位置的影响,证明了催化剂-载体附着位置对催化剂性能的关键因素,以及(ii)二氧化硅载体介孔长度的影响,证明了减少扩散限制会导致活性位的可及性增加和更高的催化剂周转率。我们在简单的填充床流动反应器中使用固定化双铑催化剂,实现了与分批使用的均相催化剂相当的产率和对映选择性,并在十个催化剂循环中保持了这种性能。