Scalable microfabricated multiphase reactors for direct fluorination reactions

N. de Mas, A. Gunther, M. Schmidt, K. Jensen
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引用次数: 6

Abstract

We report a stacked multichannel microfabricated gas-liquid reactor to carry out direct fluorination reactions with a volumetric liquid throughput of 81 ml/hr, which translates to grams per hour of fluorinated product. Fluorinated compounds are rarely synthesized by direct fluorination in conventional macroscale reactors due to the difficulties in controlling the large heat of reaction and the poor selectivity of the process. The substantial throughput and inherent safety of our microreactor makes it a promising drug discovery tool. We use pressure drop gas and liquid inlet channels to ensure uniform gas-liquid flow distribution over a large number of reaction channels operating in parallel with single gas and liquid inlet and outlet ports. Microfluidic channels are formed in a (100) silicon substrate using standard photolithographic techniques and nested potassium hydroxide etching. Twenty reaction channels are formed in each silicon layer. Gas and liquid are introduced to all layers through vertical fluidic connections. Alternate layers of drilled Pyrex are anodically bonded to the silicon to provide the vertical fluidic connections. Fluorescence microscopy of the gas-liquid flow regimes obtained in individual reaction channels indicates uniform flow distribution within one reaction layer and across different layers.
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用于直接氟化反应的可伸缩微制造多相反应器
我们报告了一种堆叠多通道微制造气液反应器,用于进行直接氟化反应,其体积液体通量为81 ml/hr,相当于每小时氟化产物的克数。由于难以控制大的反应热和工艺的选择性差,在常规的大型反应器中直接氟化合成含氟化合物的方法很少。微反应器的高通量和固有安全性使其成为一种很有前途的药物发现工具。我们采用压降气液进口通道,以确保在单个气液进出口口平行运行的大量反应通道上均匀的气液流动分布。使用标准光刻技术和嵌套氢氧化钾蚀刻在(100)硅衬底中形成微流控通道。在每一硅层中形成20个反应通道。气体和液体通过垂直流体连接引入各层。交替层钻的耐热玻璃阳极结合到硅,以提供垂直流体连接。在单个反应通道中获得的气液流动状态的荧光显微镜显示,在一个反应层内和不同层之间的流动分布均匀。
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