Parallel reactor systems for bioprocess development

被引:61
作者
Weuster-Botz, D [1 ]
机构
[1] Tech Univ Munich, Lehrstuhl Bioverfahrenstech, D-85748 Garching, Germany
来源
TECHNOLOGY TRANSFER IN BIOTECHNOLOGY: FROM LAB TO INDUSTRY TO PRODUCTION | 2005年 / 92卷
关键词
bioprocess development; parallel bioreactors; intermittent feeding; parallel control; scale-up/scale-down;
D O I
10.1007/b98916
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Controlled parallel bioreactor systems allow fed-batch operation at early stages of process development. The characteristics of shaken bioreactors operated in parallel (shake flask, microtiter plate), sparged bioreactors (small-scale bubble column) and stirred bioreactors (stirred-tank, stirred column) are briefly summarized. Parallel fed-batch operation is achieved with an intermittent feeding and pH-control system for up to 16 bioreactors operated in parallel on a scale of 100 ml. Examples of the scale-up and scale-down of pH-controlled microbial fed-batch processes demonstrate that controlled parallel reactor systems can result in more effective bioprocess development. Future developments are also outlined, including units of 48 parallel stirred-tank reactors with individual pH- and pO(2)-controls and automation as well as liquid handling system, operated on a scale of ml.
引用
收藏
页码:125 / 143
页数:19
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