Process intensification and waste minimization for ibuprofen synthesis process

被引:17
作者
Ma, Yixin [1 ]
Zhang, Xia [2 ]
Zhu, Zhaoyou [2 ]
Wang, Yinglong [2 ]
Gao, Jun [1 ]
Cui, Peizhe [2 ]
机构
[1] Shandong Univ Sci & Technol, Coll Chem & Environm Engn, Qianwangang Rd 579, Qingdao 266590, Shangdong, Peoples R China
[2] Qingdao Univ Sci & Technol, Coll Chem Engn, Zhengzhou Rd 53, Qingdao 266042, Shangdong, Peoples R China
基金
中国国家自然科学基金;
关键词
Ibuprofen; Process intensification; Waste minimization; Reactive distillation; Reactor design;
D O I
10.1016/j.jclepro.2018.05.131
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In China, the most commonly used method for the synthesis of ibuprofen is aryl-1,2-translocation rearrangement, which comprises several main processes: the Friedel-hydrolysis reaction, ketal reaction and so on. There are some problems in the process of industrial production. The temperature control of the Friedel-hydrolysis reaction is a problem because excessive temperatures will lead to the occurrence of side reactions, and low temperatures will lead to the crystallization of raw reaction materials. The reaction time of the ketal reaction is up to 24 h, which limits the productive capacity of ibuprofen. Otherwise, the emissions of the ibuprofen synthesis processes are more than 5000 m(3)/h of waste gas with VOC contents of over 1000 mg/m(3) and highly concentrated organic wastewater, with a COD up to 20,000 mg/L. Therefore, process intensification and waste minimization of the ibuprofen synthesis process is described in this paper. A new reactor is designed for the Friedel-hydrolysis reaction. The reaction temperature can be precisely controlled at 13-15 degrees C, which effectively inhibits the occurrence of side reactions. The industrial applications showed that the ketal reaction time is reduced from 24 h to less than 8 h. The VOC content is reduced to less than 100 mg/m(3), and the COD value is reduced to 150 mg/L in the improved processes, which meet national emissions standards. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:396 / 405
页数:10
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