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- W4311492066 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 2,4-dinitroanisole was selected as the model reaction, and a variety of catalysts were utilized in the continuous flow system based on μPBR for hydrogenation of 2,4-dinitroanisole. During 960 minutes of operation, the synthesis of 2,4-diaminoanisole was carried out using a Pd (OH)2/C catalyst and the optimal process condition, yielding 100 % conversion, 99.5 % selectivity, and the favorable durability. For the hydrogenation of relevant aromatic dinitro compounds, the continuous flow system demonstrates exceptional performance." @default.
- W4311492066 created "2022-12-26" @default.
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- W4311492066 date "2022-12-14" @default.
- W4311492066 modified "2023-09-29" @default.
- W4311492066 title "Micropacked‐bed Reactor for Continuous Hydrogenation of Aromatic Dinitro Compounds" @default.
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- W4311492066 doi "https://doi.org/10.1002/slct.202203577" @default.
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