Plant cell suspension culture in a bench-scale fermenter with a newly designed membrane stirrer for bubble-free aeration

被引:8
作者
Bohme, C
Schroder, MB
JungHeiliger, H
Lehmann, J
机构
[1] TECH UNIV CAROLO WILHELMINA BRAUNSCHWEIG,INST LEBENSMITTELCHEM,D-38106 BRAUNSCHWEIG,GERMANY
[2] CELLER PFLANZEN & GEWEBELAB GMBH,D-29202 CELLE,GERMANY
关键词
Oxygen; Biomass; Mass Transfer; Transfer Coefficient; Aeration;
D O I
10.1007/s002530051030
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
In this paper, tests of an optimized membrane-stirrer geometry for bubble-free aeration of a plant cell suspension culture are described. Cell attachment and clogging of a previously described system [Piehl et al. (1988) Appl Microbiol Biotechnol 29:456-461] led to the development of a new stirrer. The volumetric oxygen transfer capacity has been measured in aqueous medium. The mass transfer coefficient, k(1)a, was 3.75 h(-1) at 25 degrees C and at a stirrer speed of 34 rpm. The overall oxygen transfer capacity was investigated with a suspension culture of Aesculus hippocastanum It was shown that the oxygen mass transfer was sufficient even at the maximum biomass of 10-12 g dry weight/l, which was obtained by using this system. Furthermore, special attention was given to medium components like C and N sources, to avoid growth limitation due to a shortage of nutrients.
引用
收藏
页码:149 / 154
页数:6
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