Seeding and constant-supersaturation control by ATR-FTIR in anti-solvent crystallization

被引:38
作者
Yu, Zai Qun
Chow, Pui Shan
Tan, Reginald B. H.
机构
[1] Natl Univ Singapore, Dept Chem & Biomol Engn, Singapore 119260, Singapore
[2] Inst Chem & Engn Sci Ltd, Singapore 627833, Singapore
关键词
D O I
10.1021/op060058j
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The strategy for seeding and supersaturation control can play a critical role in defining the purity and particle size distribution of crystal products. Previous research has demonstrated that operation of crystallizers at constant supersaturation by feedback control is attractive due to its simplicity and resistance to operating disturbances. In this study, the effects of seed loading and seed size distribution were investigated for anti-solvent crystallization of paracetamol from a water-acetone mixture operated at constant supersaturation. A seeding strategy based on a simple mass balance equation provided a good starting point for the refinement of particle size distribution and adjustment of batch time in different circumstances to obtain a target average crystal size with narrow size distribution.
引用
收藏
页码:717 / 722
页数:6
相关论文
共 26 条
[1]   Optimization of batch cooling crystallization [J].
Choong, KL ;
Smith, R .
CHEMICAL ENGINEERING SCIENCE, 2004, 59 (02) :313-327
[2]   Optimal seeding in batch crystallization [J].
Chung, SH ;
Ma, DL ;
Braatz, RD .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (03) :590-596
[3]   Mathematical modeling and optimal control strategy development for an adipic acid crystallization process [J].
Costa, CBB ;
da Costa, AC ;
Maciel, R .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2005, 44 (07) :737-753
[4]   ATR-FTIR for determining optimal cooling curves for batch crystallization of succinic acid [J].
Feng, LL ;
Berglund, KA .
CRYSTAL GROWTH & DESIGN, 2002, 2 (05) :449-452
[5]   First-principles and direct design approaches for the control of pharmaceutical crystallization [J].
Fujiwara, M ;
Nagy, ZK ;
Chew, JW ;
Braatz, RD .
JOURNAL OF PROCESS CONTROL, 2005, 15 (05) :493-504
[6]  
Genck WJ, 2000, CHEM ENG-NEW YORK, V107, P90
[7]   In-process ATR-FTIR spectroscopy for closed-loop supersaturation control of a batch crystallizer producing monosodium glutamate crystals of defined size [J].
Grön, H ;
Borissova, A ;
Roberts, KJ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (01) :198-206
[8]   Optimal control of a batch cooling seeded crystallizer [J].
Hu, Q ;
Rohani, S ;
Wang, DX ;
Jutan, A .
POWDER TECHNOLOGY, 2005, 156 (2-3) :170-176
[9]   OPTIMAL OPERATION OF A BATCH COOLING CRYSTALLIZER [J].
JONES, AG .
CHEMICAL ENGINEERING SCIENCE, 1974, 29 (05) :1075-1087
[10]   MICROCOMPUTER PROGRAMMING OF DOSAGE RATE DURING BATCH PRECIPITATION [J].
JONES, AG ;
TEODOSSIEV, NM .
CRYSTAL RESEARCH AND TECHNOLOGY, 1988, 23 (08) :957-966