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High-flux isobutanol production using engineered Escherichia coli: a bioreactor study with in situ product removal
被引:172
作者:
Baez, Antonino
[1
]
Cho, Kwang-Myung
[1
]
Liao, James C.
[1
,2
]
机构:
[1] Univ Calif Los Angeles, Dept Chem & Biomol Engn, Los Angeles, CA 90095 USA
[2] Univ Calif Los Angeles, Inst Genom & Prote, Los Angeles, CA 90095 USA
关键词:
Biofuels;
Isobutanol;
E;
coli;
Gas stripping;
Bioreactor;
ACETATE ACCUMULATION;
BIOFUEL PRODUCTION;
SYNTHETIC BIOLOGY;
ETHANOL TOLERANCE;
BUTANOL;
RECOVERY;
MUTANT;
FERMENTATION;
ALCOHOLS;
CHALLENGES;
D O I:
10.1007/s00253-011-3173-y
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:
Promising approaches to produce higher alcohols, e.g., isobutanol, using Escherichia coli have been developed with successful results. Here, we translated the isobutanol process from shake flasks to a 1-L bioreactor in order to characterize three E. coli strains. With in situ isobutanol removal from the bioreactor using gas stripping, the engineered E. coli strain (JCL260) produced more than 50 g/L in 72 h. In addition, the isobutanol production by the parental strain (JCL16) and the high isobutanol-tolerant mutant (SA481) were compared with JCL260. Interestingly, we found that the isobutanol-tolerant strain in fact produced worse than either JCL16 or JCL260. This result suggests that in situ product removal can properly overcome isobutanol toxicity in E. coli cultures. The isobutanol productivity was approximately twofold and the titer was 9% higher than n-butanol produced by Clostridium in a similar integrated system.
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页码:1681 / 1690
页数:10
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