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Strategy for the design of a bioreactor for L-lysine immobilized fermentation using Corynebacterium glutamicum.
Meng, Gang; Zhao, Wei; Liu, Qingguo; Zhao, Chunguang; Zou, Yanan; Zhao, Nan; Liu, Dong; Ying, Hanjie; Sun, Wenjun; Chen, Yong.
  • Meng G; Ningxia Yipin Biotechnology Co. Ltd, Yinchuan, China.
  • Zhao W; Nanjing Hi-Tech Biological Technology Research Institute Co. Ltd, Nanjing, China.
  • Liu Q; Nanjing Hi-Tech Biological Technology Research Institute Co. Ltd, Nanjing, China.
  • Zhao C; Ningxia Yipin Biotechnology Co. Ltd, Yinchuan, China.
  • Zou Y; Nanjing Hi-Tech Biological Technology Research Institute Co. Ltd, Nanjing, China.
  • Zhao N; Nanjing Hi-Tech Biological Technology Research Institute Co. Ltd, Nanjing, China.
  • Liu D; College of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing, China.
  • Ying H; College of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing, China.
  • Sun W; College of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing, China. sunwenjun@njtech.edu.cn.
  • Chen Y; College of Biotechnology and Pharmaceutical Engineering, Nanjing Tech University, Nanjing, China. chenyong1982@njtech.edu.cn.
Appl Microbiol Biotechnol ; 106(17): 5449-5458, 2022 Sep.
Article en En | MEDLINE | ID: mdl-35902409
ABSTRACT
Biofilm-immobilized fermentation is a novel strategy that has been utilized in L-lysine fermentation. In this study, we describe a strategy for designing bioreactors for immobilized fermentation. We have constructed steel structures in which the carriers can be sewn, forming several star-like structures with different angles, and changing the ventilation robot to the aeration tray. In a 10-L bioreactor, this structure with 12 angles assisted the immobilized system to remedy the gap between free-cell and immobilized fermentation in the conversion rate. In a 50-L bioreactor, this enlarged structure with 16 angles illustrated a 4.61% higher conversion rate than the free-cell fermentation (67.75%) and increased the production by 28.56%. This successful case is the first step towards to industrial production of biofilm-based immobilized fermentation.Key points• The designed steel structure is useful for L-lysine immobilized fermentation in a 10-L bioreactor.• The conversion rate of immobilized fermentation increased from 13.99 to 60.07% and is 1.03% higher than that of the free-cell fermentation.• The conversion rate of the redesigned 50-L bioreactor is higher than that of free-cell fermentation.
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Texto completo: 1 Banco de datos: MEDLINE Asunto principal: Corynebacterium glutamicum Idioma: En Año: 2022 Tipo del documento: Article

Texto completo: 1 Banco de datos: MEDLINE Asunto principal: Corynebacterium glutamicum Idioma: En Año: 2022 Tipo del documento: Article