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A continuous multi-stage mixed-suspension mixed-product-removal crystallization system with fines dissolution
被引:20
|作者:
Acevedo, David
[1
]
Jarmer, Daniel J.
[2
]
Burcham, Christopher L.
[2
]
Polster, Christopher S.
[2
]
Nagy, Zoltan K.
[1
]
机构:
[1] Purdue Univ, Davidson Sch Chem Engn, W Lafayette, IN 47907 USA
[2] Eli Lilly & Co, Indianapolis, IN 46285 USA
来源:
基金:
美国国家科学基金会;
关键词:
Continuous crystallization;
MSMPR;
Dissolution;
CRYSTAL SIZE DISTRIBUTION;
DIRECT NUCLEATION CONTROL;
D O I:
10.1016/j.cherd.2018.05.029
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
This work demonstrates how crystal particle size is affected by the addition of fines dissolution in a mixed suspension mixed product removal (MSMPR) cascade system. The cooling crystallization of paracetamol in water was used as a case study. Two MSMPR cascade configurations were evaluated: (i) nucleation-growth (NG), and (ii) nucleation-dissolution-growth (NDG). Simulation results demonstrate that adding a dissolution step in the MSMPR cascade configuration increases the average product crystal size. Larger crystals and a narrower distribution were obtained due to the removal of fine crystals through the continuous process. However, a small decrease in the achievable yield was observed. Experimental results also showed a similar effect on the final mean size and CSD. The results demonstrate that a dissolution stage can be optimized to increase the final crystal size and CSD by varying the dissolution temperature to optimize the CSD with minimum effect on the achievable yield. (C) 2018 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
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页码:112 / 120
页数:9
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