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
相关论文
共 29 条
[11]   Methods for intense aeration, growth, storage, and replication of bacterial strains in microtiter plates [J].
Duetz, WA ;
Rüedi, L ;
Hermann, R ;
O'Connor, K ;
Büchs, J ;
Witholt, B .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 2000, 66 (06) :2641-2646
[12]   Expression, purification and characterization of recombinant phosphomannomutase and GDP-alpha-D-mannose pyrophosphorylase from Salmonella enterica, group B, for the synthesis of GDP-alpha-D-mannose from D-mannose [J].
Elling, L ;
Ritter, JE ;
Verseck, S .
GLYCOBIOLOGY, 1996, 6 (06) :591-597
[13]   Characterization of gas-liquid mass transfer phenomena in microtiter plates [J].
Hermann, R ;
Lehmann, M ;
Büchs, J .
BIOTECHNOLOGY AND BIOENGINEERING, 2003, 81 (02) :178-186
[14]  
*I BIOCH ENG, 2004, I BIOCH ENG TU MUNCH
[15]   A dense cell culture system for aerobic microorganisms using a shaken ceramic membrane flask with surface aeration [J].
Kamoshita, Y ;
Ohashi, R ;
Suzuki, T .
JOURNAL OF FERMENTATION AND BIOENGINEERING, 1998, 85 (02) :218-222
[16]   Development of a novel box-shaped shake flask with efficient gas exchange capacity [J].
Kato, I ;
Tanaka, H .
JOURNAL OF FERMENTATION AND BIOENGINEERING, 1998, 85 (04) :404-409
[17]   Advances in understanding and modeling the gas-liquid mass transfer in shake flasks [J].
Maier, U ;
Losen, M ;
Büchs, J .
BIOCHEMICAL ENGINEERING JOURNAL, 2004, 17 (03) :155-167
[18]   Characterisation of the gas-liquid mass transfer in shaking bioreactors [J].
Maier, U ;
Büchs, J .
BIOCHEMICAL ENGINEERING JOURNAL, 2001, 7 (02) :99-106
[19]  
*OECD, 2001, APPL BIOT IND SUST, P69
[20]  
Pirt S. J., 1975, PRINCIPLES MICROBE C