2022
DOI: 10.1002/slct.202203577
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Micropacked‐bed Reactor for Continuous Hydrogenation of Aromatic Dinitro Compounds

Abstract: Due to the intricacy aromatic dinitro compound hydrogenation processes, it is difficult to attain high conversion and selectivity using merely modified catalysts in batch reactors. The micropacked-bed reactor (μPBR) offers efficient heat and mass transfer, a precise and controllable reaction process, and a high level of safety. In this work, the hydrogenation of 2,4dinitroanisole was selected as the model reaction, and a variety of catalysts were utilized in the continuous flow system based on μPBR for hydroge… Show more

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Cited by 4 publications
(2 citation statements)
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“…It is evident that the selectivity in μPBR is higher than that in batch reactors. As a result of the enhanced gas‐liquid mass transfer effect, [38] the residence time is shortened and side reactions occur less frequently, thus leading to a significant improvement in the space time yield (STY).…”
Section: Resultsmentioning
confidence: 99%
“…It is evident that the selectivity in μPBR is higher than that in batch reactors. As a result of the enhanced gas‐liquid mass transfer effect, [38] the residence time is shortened and side reactions occur less frequently, thus leading to a significant improvement in the space time yield (STY).…”
Section: Resultsmentioning
confidence: 99%
“…TDA is produced industrially using catalysts by hydrogenation of dinitrotoluene isomers 9 . The catalysts used are mainly transition metals or their compounds on various usually carbon-based supports 10 14 .…”
Section: Introductionmentioning
confidence: 99%