批处理
电解
间歇式反应器
微型反应器
电极
电化学
放大
结垢
工艺工程
泥浆
级联
连续反应器
流量(数学)
缩放比例
材料科学
流动化学
电化学电池
化学
连续流动
计算机科学
机械
电解质
色谱法
有机化学
工程类
物理
催化作用
程序设计语言
经典力学
几何学
生物化学
复合材料
膜
物理化学
数学
作者
Nikola Petrović,Bhanwar Kumar Malviya,C. Oliver Kappe,David Cantillo
标识
DOI:10.1021/acs.oprd.3c00255
摘要
Technology for the rapid scale-up of synthetic organic electrochemistry from milligrams to multigrams or multi-100 g quantities is highly desirable. Traditional parallel plate flow electrolysis cells can produce large quantities of material, but transfer from batch to this flow technology requires reoptimization of the reaction conditions and fully homogeneous reaction mixtures. Moreover, single-pass processing is often difficult to accomplish due to gas generation and the low flow rates typically used in continuous mode. Herein we present a novel reactor design, based on a rotating cylinder electrode concept, that enables seamless scale up from small scale batch experimentation to gram and even multikilogram per day quantities. The device can operate in batch and flow mode, and it is able to easily process slurries without clogging of the system or fouling of the electrodes. Continuous operation is also demonstrated using three reactors in series that act as a continuous stirred electrochemical reactor cascade, providing kilogram per day productivities in a single pass.
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