TY - JOUR
T1 - Integrating Biofilm-Based Fermentation With Continuous Processes for Improved L-Valine Production
AU - Liang, Caice
AU - Wang, Yong
AU - Shi, Shuqi
AU - Yan, Alan
AU - Liu, Qingguo
AU - Liu, Wei
AU - Han, Hui
AU - Qi, Wenlu
AU - Chen, Tianpeng
AU - Sun, Wenjun
AU - Chen, Yong
N1 - Publisher Copyright:
© 2025 Wiley-VCH GmbH.
PY - 2025/4
Y1 - 2025/4
N2 - L-valine, an essential branched-chain amino acid, is widely used across various industrial sectors. Despite its significance, there is a scarcity of continuous fermentation methodologies, specifically for L-valine production. Biofilm-based Technologies face challenges in sustaining continuous L-valine production due to cell wall damage caused by L-valine sterilization. Here, we combined continuous fermentation principles with Biofilm-based technologies to develop a biofilm-based continuous fermentation (BCF) system, enabling sustained L-valine production. By analyzing the fermentation kinetics of free-cell fermentation (FCF), we optimized the L-valine titer in BCF to 60–70 g/L, achieving a yield of 0.44 g/g glucose—a 10% increase over FCF. Notably, reducing the controlled L-valine titer in BCF extended the fermentation time but simultaneously decreased both the yield and production rate. Conversely, shortening the fermentation time was associated with an increase in both yield and production rate. In summary, BCF significantly improved L-valine purity, yield from glucose, and production rate while reducing by-product formation.
AB - L-valine, an essential branched-chain amino acid, is widely used across various industrial sectors. Despite its significance, there is a scarcity of continuous fermentation methodologies, specifically for L-valine production. Biofilm-based Technologies face challenges in sustaining continuous L-valine production due to cell wall damage caused by L-valine sterilization. Here, we combined continuous fermentation principles with Biofilm-based technologies to develop a biofilm-based continuous fermentation (BCF) system, enabling sustained L-valine production. By analyzing the fermentation kinetics of free-cell fermentation (FCF), we optimized the L-valine titer in BCF to 60–70 g/L, achieving a yield of 0.44 g/g glucose—a 10% increase over FCF. Notably, reducing the controlled L-valine titer in BCF extended the fermentation time but simultaneously decreased both the yield and production rate. Conversely, shortening the fermentation time was associated with an increase in both yield and production rate. In summary, BCF significantly improved L-valine purity, yield from glucose, and production rate while reducing by-product formation.
KW - biofilm-based continuous fermentation
KW - biofilm-based immobilized fermentation
KW - Escherichia coli
KW - free-cell fermentation
KW - L-valine
UR - http://www.scopus.com/inward/record.url?scp=105003797067&partnerID=8YFLogxK
U2 - 10.1002/biot.70027
DO - 10.1002/biot.70027
M3 - 文章
C2 - 40285394
AN - SCOPUS:105003797067
SN - 1860-6768
VL - 20
JO - Biotechnology Journal
JF - Biotechnology Journal
IS - 4
M1 - e70027
ER -