NUTRIENT-SPLIT FEEDING STRATEGY FOR DIALYSIS CULTIVATION OF ESCHERICHIA-COLI

被引:17
作者
OGBONNA, JC [1 ]
MARKL, H [1 ]
机构
[1] TECH UNIV HAMBURG,INST BIOPROC & BIOCHEM ENGN,DENICKESTR 15,W-2100 HAMBURG 90,GERMANY
关键词
HIGH CELL DENSITY CULTIVATION; ESCHERICHIA-COLI; XAD ADSORBENTS; DIALYSIS REACTOR; CONTROLLED SUBSTRATE FEED; INHIBITORY PRODUCTS; REMOVAL OF;
D O I
10.1002/bit.260411112
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
Reduction in nutrient loss during dialysis cultivation of Escherichia coli on a glycerol medium was investigated. A dialysis reactor with an inner fermentation and an outer dialysis chamber was used. Aerobic condition was maintained by limiting the glycerol feed rate to an optimum value which was estimated from the oxygen requirement for glycerol oxidation and oxygen transfer capacity of the reactor. High reduction in nutrient loss was achieved by using water as the dialyzing fluid. However, osmotic movement of water from the dialysis to the fermentation chamber was observed, and the final cell concentration was low. With a nutrient-split feeding strategy (feeding glycerol directly to the fermentation chamber and dialyzing with salt solution), glycerol loss was small, there was no osmotic flux of water to the fermentation chamber, and the cell concentration was high. Both glycerol and salt loss could be avoided, and a cell concentration of 170 g/L was obtained when the dialysis process was substituted by addition of XAD adsorbents to the dialysis chamber. Application of this nutrient-split feeding strategy to cell cultivation in a stirred tank reactor, coupled with dialysis in external dialyzer modules, resulted in low cell concentrations.
引用
收藏
页码:1092 / 1100
页数:9
相关论文
共 21 条
[1]  
BERGTER RFF, 1972, WACHSTUM MIKRO ORGAN
[2]   HIGH-CONCENTRATION CULTIVATION OF LACTOCOCCUS-CREMORIS IN A CELL-RECYCLE REACTOR [J].
BIBAL, B ;
VAYSSIER, Y ;
GOMA, G ;
PAREILLEUX, A .
BIOTECHNOLOGY AND BIOENGINEERING, 1991, 37 (08) :746-754
[3]  
CRUEGER W, 1984, BIOTECHNOLOGY TXB IN
[4]   HIGH CELL-DENSITY CULTURE OF ESCHERICHIA-COLI IN A FED BATCH SYSTEM WITH DISSOLVED-OXYGEN AS SUBSTRATE FEED INDICATOR [J].
CUTAYAR, JM ;
POILLON, D .
BIOTECHNOLOGY LETTERS, 1989, 11 (03) :155-160
[5]   APPLICATION OF AN EXTENDED KALMAN FILTER METHOD FOR MONITORING HIGH-DENSITY CULTIVATION OF ESCHERICHIA-COLI [J].
DUBACH, AC ;
MARKL, H .
JOURNAL OF FERMENTATION AND BIOENGINEERING, 1992, 73 (05) :396-402
[6]   DIALYSIS FERMENTOR SYSTEMS FOR CONCENTRATED CULTURE OF MICROORGANISMS [J].
GALLUP, DM ;
GERHARDT, P .
APPLIED MICROBIOLOGY, 1963, 11 (06) :506-&
[7]   GROWTH OF ESCHERICHIA-COLI W TO HIGH CELL CONCENTRATION BY OXYGEN LEVEL LINKED CONTROL OF CARBON SOURCE CONCENTRATION [J].
GLEISER, IE ;
BAUER, S .
BIOTECHNOLOGY AND BIOENGINEERING, 1981, 23 (05) :1015-1021
[8]   USE OF MEMBRANES TO IMPROVE BIOREACTOR PERFORMANCE [J].
HOFFMANN, H ;
SCHEPER, T ;
SCHUGERL, K ;
SCHMIDT, W .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1987, 34 (01) :B13-B19
[9]   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
[10]   SIMULTANEOUS MEASUREMENTS OF OXYGEN DIFFUSION-COEFFICIENTS AND SOLUBILITIES IN FERMENTATION MEDIA WITH POLAROGRAPHIC OXYGEN ELECTRODES [J].
JU, LK ;
HO, CS ;
BADDOUR, RF .
BIOTECHNOLOGY AND BIOENGINEERING, 1988, 31 (09) :995-1005