硝化作用
微型反应器
硫酸
产量(工程)
化学
苯
放热反应
有机化学
材料科学
催化作用
冶金
作者
Wenyuan Zhao,Qi Zhang,Wei Wei,Weichang Xu,Wenxuan Sun,Tingwang An,Ji Lu,Hande Wang,Chuan Zhou,Dongmao Yan
标识
DOI:10.1002/slct.202204997
摘要
Abstract In industry, m‐dinitrobenzene is mainly obtained by two‐step nitration of benzene, but still faces the problem of being heterogeneous and highly exothermic. In this work, a two‐step continuous‐flow nitration was developed in a microreactor, combining benzene nitration and mononitrobenzene nitration in series. The waste acid after the mononitrobenzene nitration stage was utilized in the benzene mononitration stage, and the waste acid in the benzene mononitration stage was treated and concentrated for reuse. The whole process consumes almost no sulfuric acid. Under optimal conditions, the yield of dinitrobenzene was more than 99.0 % and the selectivity of m‐dinitrobenzene was more than 91 % with a residence time of 4 min at 70 °C. In addition, the space‐time yield of the continuous microreactor was 800 times higher than the batch reactor. It provides a safe and efficient method for the industrial production of m‐dinitrobenzene.
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