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压力促进的叠氮-炔环加成反应:微量毛细管与高压釜反应器性能比较。

Pressure-accelerated azide-alkyne cycloaddition: micro capillary versus autoclave reactor performance.

机构信息

Department of Chemical Engineering and Chemistry, Micro Flow Chemistry and Process Technology, Eindhoven University of Technology, Den Dolech 2, 5612AZ, Eindhoven (The Netherlands).

出版信息

ChemSusChem. 2015 Feb;8(3):504-12. doi: 10.1002/cssc.201403034. Epub 2014 Dec 17.

Abstract

Pressure effects on regioselectivity and yield of cycloaddition reactions have been shown to exist. Nevertheless, high pressure synthetic applications with subsequent benefits in the production of natural products are limited by the general availability of the equipment. In addition, the virtues and limitations of microflow equipment under standard conditions are well established. Herein, we apply novel-process-window (NPWs) principles, such as intensification of intrinsic kinetics of a reaction using high temperature, pressure, and concentration, on azide-alkyne cycloaddition towards synthesis of Rufinamide precursor. We applied three main activation methods (i.e., uncatalyzed batch, uncatalyzed flow, and catalyzed flow) on uncatalyzed and catalyzed azide-alkyne cycloaddition. We compare the performance of two reactors, a specialized autoclave batch reactor for high-pressure operation up to 1800 bar and a capillary flow reactor (up to 400 bar). A differentiated and comprehensive picture is given for the two reactors and the three methods of activation. Reaction speedup and consequent increases in space-time yields is achieved, while the process window for favorable operation to selectively produce Rufinamide precursor in good yields is widened. The best conditions thus determined are applied to several azide-alkyne cycloadditions to widen the scope of the presented methodology.

摘要

压力对环加成反应的区域选择性和产率的影响已经得到证实。然而,由于设备的普遍可用性,高压合成应用在天然产物生产中的后续益处受到限制。此外,微流设备在标准条件下的优点和局限性已经得到很好的确立。在此,我们将新型过程窗口(NPWs)原理应用于叠氮化物-炔烃环加成反应,以强化反应的固有动力学,例如使用高温、高压和浓度来强化反应的固有动力学,从而合成 Rufinamide 前体。我们在无催化剂和催化剂存在的情况下分别应用了三种主要的激活方法(即无催化分批、无催化流动和催化流动)对叠氮化物-炔烃环加成反应进行了研究。我们比较了两种反应器的性能,一种是专门用于高压操作的高压釜间歇式反应器,压力高达 1800 巴,另一种是毛细管流动反应器,压力高达 400 巴。对于两种反应器和三种激活方法,给出了一个差异化和全面的图片。反应速度加快,时空产率相应提高,同时有利于选择性地以良好产率生产 Rufinamide 前体的操作过程窗口得到拓宽。因此确定的最佳条件应用于几种叠氮化物-炔烃环加成反应,以拓宽所提出方法的范围。

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