共 52 条
Improved production of D-pantothenic acid in Escherichia coli by integrated strain engineering and fermentation strategies
被引:37
作者:

Zou, Shuping
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Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China
Zhejiang Univ Technol, Engn Res Ctr Bioconvers & Biopurificat, Minist Educ, Hangzhou 310014, Peoples R China Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China

Zhao, Kuo
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Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China
Zhejiang Univ Technol, Engn Res Ctr Bioconvers & Biopurificat, Minist Educ, Hangzhou 310014, Peoples R China Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China

Tang, Heng
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Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China
Zhejiang Univ Technol, Engn Res Ctr Bioconvers & Biopurificat, Minist Educ, Hangzhou 310014, Peoples R China Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China

Zhang, Zheng
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Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China
Zhejiang Univ Technol, Engn Res Ctr Bioconvers & Biopurificat, Minist Educ, Hangzhou 310014, Peoples R China Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China

Zhang, Bo
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Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China
Zhejiang Univ Technol, Engn Res Ctr Bioconvers & Biopurificat, Minist Educ, Hangzhou 310014, Peoples R China Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China

Liu, Zhiqiang
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Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China
Zhejiang Univ Technol, Engn Res Ctr Bioconvers & Biopurificat, Minist Educ, Hangzhou 310014, Peoples R China Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China

Zheng, Yuguo
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机构:
Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China
Zhejiang Univ Technol, Engn Res Ctr Bioconvers & Biopurificat, Minist Educ, Hangzhou 310014, Peoples R China Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China
机构:
[1] Zhejiang Univ Technol, Coll Biotechnol & Bioengn, Key Lab Bioorgan Synth Zhejiang Prov, Hangzhou 310014, Peoples R China
[2] Zhejiang Univ Technol, Engn Res Ctr Bioconvers & Biopurificat, Minist Educ, Hangzhou 310014, Peoples R China
关键词:
Betaine;
D-pantothenic acid;
Escherichia coli;
Fermentation process;
Strain improvements;
DEHYDROGENASE COMPLEX-DEFICIENT;
L-ISOLEUCINE BIOSYNTHESIS;
CORYNEBACTERIUM-GLUTAMICUM;
EXPRESSION;
BETAINE;
ACCUMULATION;
CULTIVATION;
GLUCOSE;
GENOME;
KINASE;
D O I:
10.1016/j.jbiotec.2021.07.014
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:
D-pantothenic acid (D-PA) is an essential vitamin that has been widely used in medicine, food, and animal feed. Microbial production of D-PA from natural renewable resources is attractive and challenging. In this study, both strain improvements and fermentation process strategies were applied to achieve high-level D-PA production in Escherichia coli. First, a D-PA-producing strain was developed through deletion of the aceF and mdh genes combined with the overexpression of the gene ppnk. The obtained engineered E. coli DPA02/pT-ppnk accumulated 6.89 +/- 0.11 g/L of D-PA in shake flask fermentation, which was 79.9 % higher than the control strain. Moreover, the cultivation process contributed greatly to D-PA production with respect to titer and productivity by betaine supplementation and dissolved oxygen (DO)-feedback feeding framework. Under optimal conditions, 68.3 g/L of D-PA, the specific productivity of 0.794 g/L h and the yield of 0.36 g/g glucose in 5 L fermenter were achieved. Overall, this research successfully exploited advanced strategies to lay the foundation for bio-based DPA production in industrial applications.
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页码:65 / 72
页数:8
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