HIGH CELL-DENSITY CULTURE OF A RECOMBINANT ESCHERICHIA-COLI PRODUCING PENICILLIN ACYLASE IN A MEMBRANE CELL RECYCLE FERMENTER

被引:62
作者
LEE, YL [1 ]
CHANG, HN [1 ]
机构
[1] KOREA INST SCI & TECHNOL, DEPT CHEM ENGN, SEOUL 130650, SOUTH KOREA
关键词
D O I
10.1002/bit.260360403
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
A recombinant Escherichia coli HB101(pPAKS2) producing penicillin acylase was cultured in a membrane cell recycle fermentor. The strain was very stable throughout the whole experiment. The main inhibitory by‐product was acetic acid, and cell growth ceased when its concentration was above 14 g/L Cell density could be increased up to 145 g/L dry weight without experiencing by‐product inhibition by regulating glucose concentration in the fermentor and by using total membrane recycle. Acetic acid formation was negligible not only when cells were cultured in medium containing no glucose but also when glucose was limited. Dissolved oxygen control as well as glucose limitation was an indispensable condition for minimizing acetic acid formation when the medium contained glucose. Low concentrations of accumulated acetic acid were reused when glucose was limited. Use of highly concentrated medium reduced the membrane surface area required for cell recycle greatly. The recycle fermentor could be operated in various operational modes including partial bleed and repeated recycle culture to give high productivity. Productivity of a repeated recycle system was over 10 times higher than that of a simple batch system. Copyright © 1990 John Wiley & Sons, Inc.
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页码:330 / 337
页数:8
相关论文
共 24 条
[1]   MICROFILTRATION CULTURE PROCESS FOR ENHANCED PRODUCTION OF RDNA RECEPTOR-CELLS OF ESCHERICHIA-COLI [J].
ANDERSON, KW ;
GRULKE, E ;
GERHARDT, P .
BIO-TECHNOLOGY, 1984, 2 (10) :891-896
[2]  
BAILEY JE, 1986, BIOCH ENG FUNDAMENTA, P422
[3]   DENSE GROWTH OF AEROBIC BACTERIA IN A BENCH-SCALE FERMENTOR [J].
BAUER, S ;
ZIV, E .
BIOTECHNOLOGY AND BIOENGINEERING, 1976, 18 (01) :81-94
[4]  
FUKUDA H, 1978, J FERMENT TECHNOL, V56, P619
[5]  
FUKUDA H, 1978, J FERMENT TECHNOL, V56, P354
[6]   RAPID ETHANOL FERMENTATION OF CELLULOSE HYDROLYSATE .1. BATCH VERSUS CONTINUOUS SYSTEMS [J].
GHOSE, TK ;
TYAGI, RD .
BIOTECHNOLOGY AND BIOENGINEERING, 1979, 21 (08) :1387-1400
[7]   CONTINUOUS CULTURE WITH COMPLETE CELL RECYCLE TO OBTAIN HIGH CELL DENSITIES IN PRODUCT INHIBITED CULTURES - CULTIVATION OF STREPTOCOCCUS-LACTIS FOR PRODUCTION OF SUPEROXIDE-DISMUTASE [J].
HOLST, O ;
HANSSON, L ;
BERG, AC ;
MATTIASSON, B .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1985, 23 (01) :10-14
[8]  
KIM YC, 1983, KOREAN J MICROBIOL, V21, P95
[9]  
KOBAYASHI T, 1983, P PACHEC 83, V3, P147
[10]   REMOVAL OF INHIBITORS OF BACTERIAL-GROWTH BY DIALYSIS CULTURE [J].
LANDWALL, P ;
HOLME, T .
JOURNAL OF GENERAL MICROBIOLOGY, 1977, 103 (DEC) :345-352