Design of a Continuous Tubular Cooling Crystallizer for Process Development on Lab-Scale

被引:61
作者
Hohmann, Lukas [1 ]
Gorny, Ramona [2 ]
Klaas, Oliver [1 ]
Ahlert, Jonas [1 ]
Wohlgemuth, Kerstin [3 ]
Kockmann, Norbert [1 ]
机构
[1] TU Dortmund Univ, Dept Biochem & Chem Engn, Lab Equipment Design, Emil Figge Str 68, Dortmund, Germany
[2] TU Dortmund Univ, Dept Biochem & Chem Engn, Lab Solids Proc Engn, Dortmund, Germany
[3] TU Dortmund Univ, Dept Biochem & Chem Engn, Lab Plant & Proc Design, Dortmund, Germany
关键词
Coiled flow inverter; Continuous cooling crystallization; Product purification; Tubular device; RESIDENCE TIME DISTRIBUTION; SAFETY ASPECTS; HEAT-TRANSFER; COILED FLOW; NUCLEATION; VISCOSITY; PRESSURE; INVERTER; INDUSTRY; BATCH;
D O I
10.1002/ceat.201600072
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Continuous manufacturing of fine chemical, life science, and pharmaceutical products is under recent investigation in R&D. As cooling crystallization is an important unit operation for purification of products, continuously operated, scalable devices are required for process development on lab-scale. A tubular crystallizer was developed, based on the coiled flow inverter design. Experimental characterization proved a narrow residence time distribution of the liquid phase close to ideal plug flow. Counter-current air cooling allows for adjusting linear and curved temperature profiles. Unseeded operation with the L-alanine (water) system demonstrated that nucleation has to be actively controlled to successfully apply intensified continuous cooling crystallization processes.
引用
收藏
页码:1268 / 1280
页数:13
相关论文
共 55 条
[1]   Unusually Large Young's Moduli of Amino Acid Molecular Crystals [J].
Azuri, Ido ;
Meirzadeh, Elena ;
Ehre, David ;
Cohen, Sidney R. ;
Rappe, Andrew M. ;
Lahav, Meir ;
Lubomirsky, Igor ;
Kronik, Leeor .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2015, 54 (46) :13566-13570
[2]  
Bayer Technology Services GmbH, F3 FACT CREAT FUT PR
[3]  
Beckmann W., 2013, Crystallization: Basic Concepts and Industrial Applications, P7
[4]   Future Production Concepts in the Chemical Industry: Modular - Small-Scale - Continuous [J].
Bieringer, Thomas ;
Buchholz, Sigurd ;
Kockmann, Norbert .
CHEMICAL ENGINEERING & TECHNOLOGY, 2013, 36 (06) :900-910
[5]  
Bott TR., 1995, Fouling of Heat Exchangers
[6]   Information Technologies for Innovative Process and Plant Design [J].
Bramsiepe, Christian ;
Krasberg, Nicolai ;
Fleischer, Christoph ;
Hohmann, Lukas ;
Kockmann, Norbert ;
Schembecker, Gerhard .
CHEMIE INGENIEUR TECHNIK, 2014, 86 (07) :966-981
[7]   Seeded Crystallization of β-L-Glutamic Acid in a Continuous Oscillatory Baffled Crystallizer [J].
Briggs, Naomi E. B. ;
Schacht, Ulrich ;
Raval, Vishal ;
McGlone, Thomas ;
Sefcik, Jan ;
Florence, Alastair J. .
ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2015, 19 (12) :1903-1911
[8]   Pharmaceutical Crystallization [J].
Chen, Jie ;
Sarma, Bipul ;
Evans, James M. B. ;
Myerson, Allan S. .
CRYSTAL GROWTH & DESIGN, 2011, 11 (04) :887-895
[9]   When Solids Stop Flow Chemistry in Commercial Tubing [J].
Chen, Yizheng ;
Sabio, Jasmine C. ;
Hartman, Ryan L. .
JOURNAL OF FLOW CHEMISTRY, 2015, 5 (03) :166-171
[10]   Seed loading effects on the mean crystal size of acetylsalicylic acid in a continuous-flow crystallization device [J].
Eder, R. J. P. ;
Schmitt, E. K. ;
Grill, J. ;
Radl, S. ;
Gruber-Woelfler, H. ;
Khinast, J. G. .
CRYSTAL RESEARCH AND TECHNOLOGY, 2011, 46 (03) :227-237