Simultaneous preferential crystallization in a coupled, batch operation mode - Part 1: Theoretical analysis and optimization

被引:32
|
作者
Elsner, Martin Peter
Ziornek, Grzegorz
Seidel-Morgenstern, Andreas
机构
[1] MAx Planck Inst Dynm Complex Tech Syst, D-39106 Magdeburg, Germany
[2] Otto Von Guericke Univ, Dept Chem Engn, D-39106 Magdeburg, Germany
关键词
enantioseparation; process intensification; crystallization; crystallizer configuration; productivity; optimization;
D O I
10.1016/j.ces.2007.05.035
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The intention of this paper is the theoretical analysis and optimization of preferential crystallization of enantiomers performed simultaneously in two batch crystallizers which are coupled. An exchange of the liquid phases may increase the overall crystallization kinetics and that might lead to a higher productivity. In this study, the amino acid threonine dissolved in water was used as a model system. Taking experimentally estimated parameters describing the crystallization thermodynamics as well as kinetics into consideration, a simplified mathematical description based on population balance model was established for the simulation of the time changes of liquid phase composition during the preferential crystallization process. Based on this simplified model the above mentioned crystallizer configurations has been optimized and investigated concerning the maximum attainable productivity. (C) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4760 / 4769
页数:10
相关论文
共 50 条
  • [1] Simultaneous preferential crystallization in a coupled batch operation mode. Part II: Experimental study and model refinement
    Elsner, Martin Peter
    Ziomek, Grzegorz
    Seidel-Morgenstern, Andreas
    [J]. CHEMICAL ENGINEERING SCIENCE, 2011, 66 (06) : 1269 - 1284
  • [2] Theoretical investigation of simultaneous continuous preferential crystallization in a coupled mode
    Qamar, Shamsul
    Galan, Kamila
    Elsner, Martin Peter
    Hussain, Iltaf
    Seidel-Morgenstern, Andreas
    [J]. CHEMICAL ENGINEERING SCIENCE, 2013, 98 : 25 - 39
  • [3] Solutions to inversion problems in preferential crystallization of enantiomers-Part II: Batch crystallization in two coupled vessels
    Hofmann, Steffen
    Raisch, Joerg
    [J]. CHEMICAL ENGINEERING SCIENCE, 2013, 88 : 48 - 68
  • [4] Optimal operation of enantioseparation by batch-wise preferential crystallization
    Angelov, I.
    Raisch, J.
    Elsner, M. P.
    Eidel-Morgenstern, A. S.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2008, 63 (05) : 1282 - 1292
  • [5] Solutions to inversion problems in preferential crystallization of enantiomers-part I: Batch crystallization in a single vessel
    Hofmann, Steffen
    Raisch, Joerg
    [J]. CHEMICAL ENGINEERING SCIENCE, 2012, 80 : 253 - 269
  • [6] Simultaneous Optimization of the Design and Operation of Batch Reactive Distillation Processes
    Kao, Yu-Lung
    Ward, Jeffrey D.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2016, 55 (01) : 267 - 278
  • [7] Shortcut Model for Batch Preferential Crystallization Coupled with Racemization for Conglomerate-Forming Chiral Systems
    Bhandari, Shashank
    Carneiro, Thiane
    Lorenz, Heike
    Seidel-Morgenstern, Andreas
    [J]. CRYSTAL GROWTH & DESIGN, 2022, 22 (07) : 4094 - 4104
  • [8] Diastereomeric salt crystallization of chiral molecules via sequential coupled-Batch operation
    Simon, Melba
    Wood, Barbara
    Ferguson, Steven
    Glennon, Brian
    Jones, Roderick C.
    [J]. AICHE JOURNAL, 2019, 65 (02) : 604 - 616
  • [9] Optimization of cooling strategy and seeding by FBRM analysis of batch crystallization
    Zhang, Dejiang
    Liu, Lande
    Xu, Shijie
    Du, Shichao
    Dong, Weibing
    Gong, Junbo
    [J]. JOURNAL OF CRYSTAL GROWTH, 2018, 486 : 1 - 9
  • [10] Simultaneous optimization of feeding rate and operation parameters for fed-batch fermentation processes
    Wang, FS
    Cheng, WM
    [J]. BIOTECHNOLOGY PROGRESS, 1999, 15 (05) : 949 - 952