Designs of continuous-flow pharmaceutical crystallizers: developments and practice

被引:104
作者
Jiang, Mo [1 ,2 ]
Braatz, Richard D. [1 ]
机构
[1] MIT, Dept Chem Engn, 77 Massachusetts Ave,E19-551, Cambridge, MA 02139 USA
[2] Virginia Commonwealth Univ, Dept Chem & Life Sci Engn, Richmond, VA 23219 USA
关键词
CONTINUOUS MIXED-SUSPENSION; CONTROLLING PARTICLE-SIZE; OF-THE-ART; CONTINUOUS SONOCRYSTALLIZATION; TUBULAR CRYSTALLIZATION; PROCESS INTENSIFICATION; MSMPR CRYSTALLIZATION; SCALE-UP; PRODUCT; NUCLEATION;
D O I
10.1039/c8ce00042e
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Crystallization is an effective, low-cost purification & formulation process widely applied to pharmaceuticals and fine chemicals. This review describes recent advances in research on lab-scale solution-based continuous crystallization, including (1) a 5-step general design procedure; (2) key design/ operational parameters; (3) process intensification strategies; and (4) a case study. The continuous crystallizers reviewed include mixed-suspension mixed-product removal, fluidized beds, oscillatory baffled flow, and tubular laminar/ segmented/ slug-flow crystallizers. Their corresponding design and operational considerations are summarized in terms of general parameters (e. g., residence time), and crystallizer-specific parameters and strategies (e. g., mixing strategies). In-line nucleation and crystal modification methods are categorized, including use of micromixers, wet milling, ultrasonication, temperature cycling, and recycling selection (filtration, sedimentation). Throughout the article, links are drawn with extensive existing knowledge of batch crystallizers, to facilitate the understanding and design of continuous crystallizers.
引用
收藏
页码:3534 / 3551
页数:18
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