首页> 外国专利> Adiabatic nitration of benzene, comprises reacting nitric acid and benzene in presence of sulfuric acid to nitrobenzene, concentrating the diluted sulfuric acid, cooling and purifying crude nitrobenzene and distilling washed nitrobenzene

Adiabatic nitration of benzene, comprises reacting nitric acid and benzene in presence of sulfuric acid to nitrobenzene, concentrating the diluted sulfuric acid, cooling and purifying crude nitrobenzene and distilling washed nitrobenzene

机译:苯的绝热硝化,包括在硫酸存在下使硝酸和苯与硝基苯反应,浓缩稀硫酸,冷却并纯化粗硝基苯,然后蒸馏洗涤过的硝基苯

摘要

Adiabatic nitration of benzene, comprises: (a) reacting nitric acid (1) and benzene (2) in a reactor in presence of sulfuric acid (3) to obtain nitrobenzene; (b) separating the hot reaction mixture in a separator; (c) concentrating the diluted sulfuric acid obtained during the reaction; (d) cooling the crude nitrobenzene (5); (e) purifying the crude nitrobenzene in a multi-step washing process; and (f) distilling the washed nitrobenzene to separate the low boilers and remaining water. The separation of crude nitrobenzene and sulfuric acid is carried out under pressure. Adiabatic nitration of benzene, comprises: (a) reacting nitric acid (1) and benzene (2) in a reactor in presence of sulfuric acid (3) to obtain nitrobenzene; (b) separating the hot reaction mixture in a separator; (c) concentrating the diluted sulfuric acid obtained during the reaction; (d) cooling the crude nitrobenzene (5); (e) purifying the crude nitrobenzene in a multi-step washing process; and (f) distilling the washed nitrobenzene to separate the low boilers and remaining water. The separation of crude nitrobenzene and sulfuric acid is carried out under pressure. The pressure is maintained using a pressure maintaining siphon. The benzene and low boiling mixture obtained during the distillation are separated from the remaining water. A portion of the resulting benzene and the low boiling mixture are discharged and the benzene and the low boiling mixture are then recycled for nitration.
机译:苯的绝热硝化包括:(a)使硝酸(1)和苯(2)在反应器中在硫酸(3)的存在下反应以获得硝基苯; (b)在分离器中分离热反应混合物; (c)浓缩反应过程中得到的稀硫酸; (d)冷却粗硝基苯(5); (e)在多步洗涤过程中纯化粗硝基苯; (f)蒸馏洗涤过的硝基苯以分离低沸物和剩余的水。粗硝基苯和硫酸的分离在压力下进行。苯的绝热硝化包括:(a)使硝酸(1)和苯(2)在反应器中在硫酸(3)的存在下反应以获得硝基苯; (b)在分离器中分离热反应混合物; (c)浓缩反应过程中得到的稀硫酸; (d)冷却粗硝基苯(5); (e)在多步洗涤过程中纯化粗硝基苯; (f)蒸馏洗涤过的硝基苯以分离低沸物和剩余的水。粗硝基苯和硫酸的分离在压力下进行。使用压力保持虹吸管保持压力。将蒸馏过程中获得的苯和低沸点混合物与剩余的水分离。排出一部分所得苯和低沸点混合物,然后将苯和低沸点混合物再循环用于硝化。

著录项

  • 公开/公告号DE102009005324A1

    专利类型

  • 公开/公告日2010-07-22

    原文格式PDF

  • 申请/专利权人 PLINKE GMBH;

    申请/专利号DE20091005324

  • 申请日2009-01-16

  • 分类号C07C205/04;

  • 国家 DE

  • 入库时间 2022-08-21 18:28:27

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