Coupling of Heck and hydrogenation reactions in a continuous compact reactor

被引:34
作者
Fan, Xiaolei [1 ]
Manchon, Maria Gonzalez [1 ]
Wilson, Karen [2 ]
Tennison, Steve [3 ]
Kozynchenko, Alexander [3 ]
Lapkin, Alexei A. [1 ]
Plucinski, Pawel K. [1 ]
机构
[1] Univ Bath, Dept Chem Engn, Ctr Sustainable Chem Technol, Bath BA2 7AY, Avon, England
[2] Univ York, Dept Chem, York YO10 5DD, N Yorkshire, England
[3] MAST Carbon Int Ltd, Surrey GU3 2AF, England
基金
英国工程与自然科学研究理事会;
关键词
Flow chemistry; Compact reactors; Multifunctional reactors; Tandem reactions; SUPPORTED PALLADIUM CATALYSTS; LIQUID-PHASE OXIDATION; MULTISTEP SYNTHESIS; METHYL ACRYLATE; IODOBENZENE; TECHNOLOGY; BASES;
D O I
10.1016/j.jcat.2009.07.019
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
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. (C) 2009 Elsevier Inc. All rights reserved.
引用
收藏
页码:114 / 120
页数:7
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