OXYGEN-TRANSFER RATES IN A MAMMALIAN-CELL CULTURE BIOREACTOR EQUIPPED WITH A CELL-LIFT IMPELLER

被引:34
作者
JOHNSON, M [1 ]
ANDRE, G [1 ]
CHAVARIE, C [1 ]
ARCHAMBAULT, J [1 ]
机构
[1] NATL RES COUNCIL CANADA,BIOTECHNOL RES INST,MONTREAL H4P 2R2,QUEBEC,CANADA
关键词
D O I
10.1002/bit.260350107
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
Measurements of kLa were carried out in 1. 5‐ and 5‐L New Brunswick Scientific CelliGen® bioreactors. The measured kLa in water were identical for both vessel sizes operated in similar condition. The mass transfer rate increased with temperature, mixing speed, and aeration rate, with this last parameter being the most significant. Surface aeration alone gave kLa values of 0. 4 to 1. 6 h−1. A 25% decrease in kLa was observed above an aeration rate of 1. 6 vvm. This was caused by the particular foam breaker of the CelliGen bioreactor. Measurements of kLa using a mammalian cell culture medium supplemented with 5% fetal calf serum (FCS) have confirmed the negative effect of the foam breaker on kLa The measured value in this medium was 1. 2 h−1 for all aeration rates, more than 60% of which was attributed to surface aeration. Copyright © 1990 John Wiley & Sons, Inc.
引用
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页码:43 / 49
页数:7
相关论文
共 8 条
[1]  
BENEFIELD LD, 1980, BIOL PROCESS DESIGN, P281
[2]  
DECKWER WD, 1974, CHEM ENG SCI, V29, P2177, DOI 10.1016/0009-2509(74)80025-4
[3]   OXYGEN-TRANSFER IN ANIMAL-CELL CULTURE-MEDIUM [J].
LAVERY, M ;
NIENOW, AW .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 30 (03) :368-373
[4]  
REUVENY S, 1986, AM BIOTECHNOL LA JAN, P28
[5]  
ROBINSON CW, 1971, THESIS U CALIFORNIA
[6]  
Sobotka M, 1982, ANN REPORTS FERMENTA, P127
[7]  
[No title captured]
[8]  
1987, INSTRUCTION MANUAL C