Optimization of L-phenylalanine production of Corynebacterium glutamicum under product feedback inhibition by elevated oxygen transfer rate

被引:20
作者
Shu, CH [1 ]
Liao, CC
机构
[1] Natl Cent Univ, Dept Chem Engn, Chungli 320, Taiwan
[2] Food Ind Res & Dev Inst, Hsinchu 300, Taiwan
关键词
Corynebacterium glutamicum; phenylalanine; product inhibition; oxygen supply;
D O I
10.1002/bit.10125
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
Production feedback inhibition both on cell growth and on product formation of phenylalanine fermentation might be alleviated by elevated oxygen supply. Batch fermentations by a high phenylalanine producing strain Corynebacterium glutamicum CCRC 18335 at various initial phenylalanine concentrations (PO) ranging from 0 to 20 g/L and different oxygen transfer rate coefficients (K(L)a) ranging from 23 to 76 h(-1) were studied. The fermentation parameters with respect to P-0 were strongly dependent on K(L)a. Cell yield favored higher K(L)a and lower P-0. Product yield with respect to varying phenylalanine concentration was evaluated by the relative oxygen availability (ROA). The optimal ROA for phenylalanine formation was strongly dependent on the product concentration. While P-0 was low, the product inhibition was less significant and the maximum product yield occurred while ROA was at 0.5-0.6. While P-0 was high, the product inhibition was significant and the maximum product yield occurred while ROA was at 0.8-0.9. These results suggest that the product feedback inhibition of phenylalanine fermentation processes can be alleviated by a gradual increase in oxygen supply rate while the increasing product concentration is taken into account. The strategy is demonstrated in a fed-batch culture with elevated oxygen supply. The final phenylalanine concentration was 23.2 g/L, which was 45% better than that of the fed-batch fermentation without elevated oxygen supply. Likewise, the maximum productivity was improved by 42% at 0.37 g/(L (.) h). (C) 2002 John Wiley Sons, Inc.
引用
收藏
页码:131 / 141
页数:11
相关论文
共 30 条
[1]  
AKASHI K, 1979, J FERMENT TECHNOL, V57, P321
[2]   EFFECT OF OXYGEN-SUPPLY ON L-LYSINE, L-THREONINE AND L-ISOLEUCINE FERMENTATIONS [J].
AKASHI, K ;
SHIBAI, H ;
HIROSE, Y .
AGRICULTURAL AND BIOLOGICAL CHEMISTRY, 1979, 43 (10) :2087-2092
[3]   GENETIC-ENGINEERING OF METABOLIC PATHWAYS APPLIED TO THE PRODUCTION OF PHENYLALANINE [J].
BACKMAN, K ;
OCONNOR, MJ ;
MARUYA, A ;
RUDD, E ;
MCKAY, D ;
BALAKRISHNAN, R ;
RADJAI, M ;
DIPASQUANTONIO, V ;
SHODA, D ;
HATCH, R ;
VENKATASUBRAMANIAN, K .
ANNALS OF THE NEW YORK ACADEMY OF SCIENCES, 1990, 589 :16-24
[4]  
Bailey JE., 1986, BIOCH ENG FUNDAMENTA, P421
[5]  
BUCKLAND B, 1985, BIO-TECHNOL, V3, P982, DOI 10.1038/nbt1185-982
[6]   Cloning of m-fluorophenylalanine-resistant gene and mutational analysis of feedback-resistant prephenate dehydratase from Corynebacterium glutamicum [J].
Chan, MS ;
Hsu, WH .
BIOCHEMICAL AND BIOPHYSICAL RESEARCH COMMUNICATIONS, 1996, 219 (02) :537-542
[7]   CONTINUOUS PRODUCTION OF PHENYLALANINE USING AN ESCHERICHIA-COLI REGULATORY MUTANT [J].
CHOI, YJ ;
TRIBE, DE .
BIOTECHNOLOGY LETTERS, 1982, 4 (04) :223-228
[8]   CORRELATION OF THEORETICAL AND EXPERIMENTAL YIELDS OF PHENYLALANINE FROM NON-GROWING CELLS OF A REC ESCHERICHIA-COLI STRAIN [J].
FORBERG, C ;
ELIAESON, T ;
HAGGSTROM, L .
JOURNAL OF BIOTECHNOLOGY, 1988, 7 (04) :319-332
[9]   PILOT-SCALE PRODUCTION OF L-PHENYLALANINE FROM D-GLUCOSE [J].
GIL, GH ;
KIM, SR ;
BAE, JC ;
LEE, JH .
ENZYME AND MICROBIAL TECHNOLOGY, 1985, 7 (08) :370-372
[10]   BIOSYNTHETIC CONTROL IN AROMATIC AMINO-ACID PRODUCING MUTANTS OF CORYNEBACTERIUM-GLUTAMICUM [J].
HAGINO, H ;
NAKAYAMA, K .
AGRICULTURAL AND BIOLOGICAL CHEMISTRY, 1975, 39 (02) :351-361