Herein we demonstrate ap acked bed flow reactor capable of achieving highly regio-and stereoselective CÀH functionalization reactions using an ewly developed Rh 2 (S-2-Cl-5-CF 3 TPCP) 4 catalyst. To optimize the immobilized dirhodium catalyst employed in the flowr eactor,w es ystematically study both (i)t he effects of ligand immobilization position, demonstrating the critical factor that the catalyst-support attachment location can have on the catalyst performance, and (ii)s ilica support mesopore length, demonstrating that decreasing diffusional limitations leads to increased accessibility of the active site and higher catalyst turnover frequency. We employt he immobilized dirhodium catalyst in as imple 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.