A Silica‐Supported Yttrium Triflate Packed Bed Reactor for Continuous Flow Michael Addition of Indoles to Benzylidene Malonates
作者:Emanuela Donato、Valerio Chiroli、Alessandra Puglisi、Maurizio Benaglia
DOI:10.1002/adsc.202301210
日期:2024.2.20
The catalytic properties of packed bed reactors filled with Y(OTf)3 immobilised onto functionalised silica have been tested in the Michael addition of indoles to benzylidene malonates under flow conditions, providing improved productivity over the batch conditions, a greater ease of recovery of the final products and a prolonged life of the catalyst. Noteworthy, the same catalytic reactor, after being
填充床反应器填充有固定在功能化二氧化硅上的 Y(OTf)3 的催化性能已经在流动条件下吲哚与亚苄基丙二酸酯的迈克尔加成中进行了测试,与间歇条件相比提供了更高的生产率,更容易回收最终产物。产品和催化剂的使用寿命延长。值得注意的是,同一个催化反应器在使用五天后,被用来进行不同的反应,即流动中的立体选择性狄尔斯阿尔德环加成反应,与间歇反应相比,生产率提高了 24 倍。