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2,4-二硝基-6-溴苯胺连续重氮化的工艺研究 被引量:4

Continuous process for diazotization of 2,4-dinitro-6-bromoaniline
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摘要 采用具有脉冲变径结构的微通道反应器,以2,4-二硝基-6-溴苯胺为原料,质量分数40%NOHSO 4为重氮化试剂,连续合成了2,4-二硝基-6-溴苯胺重氮盐。考察了2,4-二硝基-6-溴苯胺摩尔比、反应温度、98%H_(2)SO_(4)用量、停留时间等因素对重氮化反应的影响。通过实验确定较优工艺条件为:2,4-二硝基-6-溴苯胺与40%NOHSO 4摩尔比为1∶1.01,98%H_(2)SO_(4)用量为2,4-二硝基-6-溴苯胺2倍,反应温度为70℃,停留时间为250 s。该条件下,2,4-二硝基-6-溴苯胺转化率达99.4%,重氮盐选择性达96.9%。与已报道的间歇工艺相比,连续流工艺大幅缩短了反应时间,提高了重氮盐的纯度,具有一定的工业化应用前景。 2,4-dinitro-6-bromoaniline diazonium sulfate was continuously synthesized in microchannel reactor with pulse varying diameter structure,and 2,4-dinitro-6-bromoaniline and 40%NOHSO 4 were used as raw material and diazotization reagent separately.The effects of molar ratio of 2,4-dinitro-6-bromoaniline,temperature,98%H_(2)SO_(4) dosage and residence time on diazotization were investigated.The optimum conditions are determined as follows:the molar ratio of 2,4-dinitro-6-bromoaniline diazonium to 40%NOHSO 4 is 1∶1.01,the dosage of 98%H_(2)SO_(4) is 2 times compared with that of raw material,the reaction temperature is 70℃,the residence time is 250 s.Under this condition,the conversion and the selectivity can reach 99.4%and 96.9%,respectively.Compared with reported batch processes,the continuous flow process described greatly shortens reaction time,improves purity of diazonium sulfate,and has a certain industrial application prospect.
作者 张万圣 张跃 严生虎 刘建武 沈介发 ZHANG Wan-sheng;ZHANG Yue;YAN Sheng-hu;LIU Jian-wu;SHEN Jie-fa(School of Petrochemical Engineering,Changzhou University,Changzhou 213164,Jiangsu Province,China;Continuous Flow Engineering Laboratory of National Petroleum and Chemical Industry,Changzhou 213164,Jiangsu Province,China)
出处 《化学工程》 CAS CSCD 北大核心 2021年第7期56-60,共5页 Chemical Engineering(China)
关键词 2 4-二硝基-6-溴苯胺 重氮化 连续流 微通道反应器 2,4-dinitro-6-bromoaniline diazotization continuous flow microchannel reactor
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  • 1郑亚锋,赵阳,辛峰.微反应器研究及展望[J].化工进展,2004,23(5):461-467. 被引量:56
  • 2LiShL,ChenGW,SunJL,LiHQ. (ChinJCatal) . 2002
  • 3Wengen R S,Drost M K,Brenchley D L.In: Ehrfeld W ed.Proceedings of the 3rd International Conference on Microreaction Technology[].Frankfurt.1999
  • 4Service R F. Science . 1998
  • 5Jensen K F. American Institute of Chemical Engineers Journal . 1999
  • 6Tonkovich A Y,Zilka J L,LaMont M J,Wang Y,Wegeng R S. Chemical Engineering Science . 1999
  • 7Choi Y,Stenger H G. Applied Catalysis B Environmental . 2002
  • 8PROTASOVA L N,BULUT M,ORMEROD D,et al. Latest highlights in liquid-phase reactions for organic synthesis in microreactors[J]. Organic Process Research & Development,2013, 17(5):760.
  • 9FLETCHER P D I,HASWELL S J,VILLAR P E,et al. Micro reactors:principles and applications in organic synthesis[J]. Tetrahedron,2002,58(39):4735-4736.
  • 10GEYER K,CODéE J D,SEEBERGER P H. Microreactors as tools for synthetic chemists-the chemists' round-bottomed flask of the 21st century?[J]. Chemistry——A European Journal,2007,38(2):8434-8442.

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