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Coupling of Heck and hydrogenation reactions in a continuous compact reactor

机译:连续紧凑反应器中的Heck与氢化反应的耦合

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A continuous multi-step synthesis of 1,2-diphenylethane was performed sequentially in a structured compact reactor. This process involved a Heck C-C coupling reaction followed by the addition of hydrogen to perform reduction of the intermediate obtained in the first step. Both of the reactions were catalysed by microspherical carbon-supported Pd catalysts. Due to the integration of the micro-heat exchanger, the static mixer and the mesoscale packed-bed reaction channel, the compact reactor was proven to be an intensified tool for promoting the reactions. In comparison with the batch reactor, this flow process in the compact reactor was more efficient as: (i) the reaction time was significantly reduced (ca. 7 min versus several hours), (ii) no additional ligands were used and (iii) the reaction was run at lower operational pressure and temperature. Pd leached in the Heck reaction step was shown to be effectively recovered in the following hydrogenation reaction section and the catalytic activity of the system can be mostly retained by reverse flow operation.
机译:在结构紧凑的反应器中依次进行1,2-二苯乙烷的连续多步合成。该过程涉及Heck C-C偶联反应,然后加入氢以还原第一步中获得的中间体。这两个反应均由微球形碳载Pd催化剂催化。由于集成了微型热交换器,静态混合器和中型填充床反应通道,因此紧凑型反应器被证明是促进反应的增强工具。与分批反应器相比,紧凑型反应器中的这种流动过程效率更高:(i)反应时间显着减少(约7分钟,而数小时),(ii)不使用其他配体,并且(iii)反应在较低的操作压力和温度下进行。已证明在Heck反应步骤中浸出的Pd可在随后的氢化反应段中有效回收,并且该体系的催化活性可通过逆流操作大部分保留。

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