Continuous reactive crystallization of pharmaceuticals using impinging jet mixers

被引:27
作者
Liu, Wen J. [1 ,3 ]
Ma, Cai Y. [1 ]
Liu, Jing J. [2 ]
Zhang, Yang [2 ]
Wang, Xue Z. [1 ,2 ]
机构
[1] Univ Leeds, Sch Chem & Proc Engn, Leeds LS2 9JT, W Yorkshire, England
[2] South China Univ Technol, Sch Chem & Chem Engn, Guangzhou 510640, Guangdong, Peoples R China
[3] China Univ Petr, Beijing, Peoples R China
基金
英国工程与自然科学研究理事会; 中国国家自然科学基金;
关键词
reactive crystallization; continuous crystallization; continuous processing of pharmaceuticals; impinging jet mixer; process analytical technology; sodium cefuroxime; CALCIUM-CARBONATE; PARTICLE-SIZE; MULTIPLICITY PATTERNS; POPULATION BALANCE; NANO-MATERIALS; SCALE-UP; SIMULATION; STRUVITE; FBRM; PRECIPITATION;
D O I
10.1002/aic.15438
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
For reactive crystallization of pharmaceuticals that show a rapid reaction rate, low solubility of active pharmaceutical ingredient and hence a large supersaturation, it was found in a recent study that a process design which integrates an impinging jet mixer and batch stirred tank produces high quality crystals. The current investigation examines if the short processing time of reactive crystallization permits the impinging jet mixerstirred tank design to be modified to operate in a continuous mode. The new design combines an impinging jet mixer for feed introduction and reaction with a continuous stirred tank reactor (CSTR) and tubular reactor for crystal growth. A study of reactive crystallization of sodium cefuroxime (an antibiotic), using first a 1L CSTR then scaling to a 50L CSTR, found that the new design produces crystals of higher crystallinity, narrower particle size, and improved product stability, than batch crystallizers. (c) 2016 American Institute of Chemical Engineers AIChE J, 63: 967-974, 2017
引用
收藏
页码:967 / 974
页数:8
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