Simulation of antisolvent crystallization in impinging jets with coupled multiphase flow-micromixing-PBE

被引:31
作者
Cheng, Jingcai [1 ]
Yang, Chao [1 ,2 ]
Jiang, Mo [3 ]
Li, Qian [1 ,2 ]
Mao, Zai-Sha [1 ]
机构
[1] Chinese Acad Sci, Inst Proc Engn, Key Lab Green Proc & Engn, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
[3] MIT, Dept Chem Engn, Cambridge, MA 02139 USA
基金
中国国家自然科学基金;
关键词
Antisolvent crystallization; High-resolution finite-volume scheme; Population balance equation; Micromixing; OpenFOAM; POPULATION BALANCE-EQUATIONS; COMPUTATIONAL FLUID-DYNAMICS; CONTINUOUS PRECIPITATION; BARIUM-SULFATE; SCALE-UP; AGGREGATION; GROWTH; NUCLEATION; BREAKAGE; DISCRETIZATION;
D O I
10.1016/j.ces.2017.06.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The KT (Kurganov and Tadmor, 2000) finite-volume central scheme is one of the most promising high resolution numerical methods to solve the widely-used population balance equation (PBE) in crystallization and other areas. To meet the practical purpose of geometric-type particle size grid, the primary KT scheme was extended to a general form and validated for pure growth in homogeneous systems. Based on the extended KT scheme, a solver was developed that couples the general discretized PBE and ami-cromixing and a CFD mixture model in OpenFOAM (open-source field operation and manipulation). The simulation uses published parameters from and is compared to experimental antisolvent crystallization of lovastatin from a methanol-water mixture in an impinging jet. The effect of the existing solid crystals on some crystal properties is investigated in this work for the first time. The shapes of crystal size distribution (CSD) at various jet velocities are consistent with experimental observations. The geometric particle size partition is shown to be capable of improving the accuracy of simulation in divisions of the highest particle number densities or steep gradients in the number density. The existing solid crystals are also shown to have a non-negligible effect on the slurry flow crystallization systems once the mean crystal size reaches 20 mu m. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:500 / 512
页数:13
相关论文
共 46 条
[11]  
Green D. W., 2002, HDB IND CRYSTALLIZAT
[12]   Parallel high-resolution finite volume simulation of particulate processes [J].
Gunawan, Rudiyanto ;
Fusman, Irene ;
Braatz, Richard D. .
AICHE JOURNAL, 2008, 54 (06) :1449-1458
[13]  
Jasak H, 1999, INT J NUMER METH FL, V31, P431, DOI 10.1002/(SICI)1097-0363(19990930)31:2<431::AID-FLD884>3.0.CO
[14]  
2-T
[15]   Effect of jet velocity on crystal size distribution from antisolvent and cooling crystallizations in a dual impinging jet mixer [J].
Jiang, Mo ;
Li, Yao-En David ;
Tung, Hsien-Hsin ;
Braatz, Richard D. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2015, 97 :242-247
[16]   Techniques for the reconstruction of a distribution from a finite number of its moments [J].
John, V. ;
Angelov, I. ;
Oencuel, A. A. ;
Thevenin, D. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (11) :2890-2904
[17]   Chemical processing and micromixing in confined impinging jets [J].
Johnson, BK ;
Prud'homme, RK .
AICHE JOURNAL, 2003, 49 (09) :2264-2282
[18]   Process modelling tools for continuous and batch organic crystallization processes including application to scale-up [J].
Kougoulos, E. ;
Jones, A. G. ;
Wood-Kaczmar, M. W. .
ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2006, 10 (04) :739-750
[19]   Improved accuracy and convergence of discretized population balance for aggregation:: The cell average technique [J].
Kumar, J ;
Peglow, M ;
Warnecke, G ;
Heinrich, S ;
Mörl, L .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (10) :3327-3342
[20]   An efficient numerical technique for solving population balance equation involving aggregation, breakage, growth and nucleation [J].
Kumar, Jitendra ;
Peglow, Mirko ;
Warnecke, Gerald ;
Heinrich, Stefan .
POWDER TECHNOLOGY, 2008, 182 (01) :81-104