Wang Xuanlin, Miao Yingchun, Liu Weifeng, Tao Yong
CAS Key Laboratory of Microbial Physiological and Metabolic Engineering, State Key Laboratory of Microbial Resources, Institute of Microbiology, Chinese Academy of Sciences, Beijing 100101, China.
College of Life Science, University of Chinese Academy of Sciences, Beijing 100049, China.
Int J Mol Sci. 2025 Jul 14;26(14):6727. doi: 10.3390/ijms26146727.
The production of β-alanine from fatty acid feedstocks presents a promising synthetic strategy due to its high carbon yield. However, the excessive reducing power generated during fatty acid utilization disrupts cellular redox balance, adversely affecting metabolism and limiting the efficiency and final yield of β-alanine production. To address this challenge, we engineered a co-production system in which excess reducing equivalents generated during fatty acid β-oxidation and β-alanine biosynthesis were consumed by growth-coupled lycopene biosynthesis. The resulting dual-pathway strain, SA01, achieved 44.78 g/L β-alanine and 3.07 g/L lycopene in bioreactor fermentation, representing a 21.45% increase in β-alanine production compared to the β-alanine-producing strain WA01, and a 74.43% increase in lycopene production compared to the lycopene-producing strain LA01. Further optimization in strain SA06, involving cofactor engineering to shift redox flow from NADH to NADPH, enhanced the titers to 52.78 g/L β-alanine and 3.61 g/L lycopene. Metabolite analysis confirmed a decrease in intracellular NADH and FADH levels in SA06, indicating restoration of redox balance during the late fermentation phase. Additional improvements in the fermentation process, including gradual carbon source switching, optimization of the induction strategy, and fine-tuning of conditions during both growth and bioconversion phases, resulted in further increases in product titers, reaching 72 g/L β-alanine and 6.15 g/L lycopene. This study offers valuable insights into the development of microbial co-production systems, highlighting the critical role of dynamic cofactor and redox balance management, as well as process optimization, in improving production efficiency.
由于β-丙氨酸的高碳产率,利用脂肪酸原料生产β-丙氨酸是一种很有前景的合成策略。然而,脂肪酸利用过程中产生的过量还原力会破坏细胞的氧化还原平衡,对代谢产生不利影响,并限制β-丙氨酸生产的效率和最终产量。为应对这一挑战,我们构建了一个联产系统,其中脂肪酸β-氧化和β-丙氨酸生物合成过程中产生的过量还原当量通过与生长偶联的番茄红素生物合成被消耗掉。由此产生的双途径菌株SA01在生物反应器发酵中实现了44.78 g/L的β-丙氨酸和3.07 g/L的番茄红素,与生产β-丙氨酸的菌株WA01相比,β-丙氨酸产量提高了21.45%,与生产番茄红素的菌株LA01相比,番茄红素产量提高了74.43%。在菌株SA06中进行的进一步优化,包括通过辅因子工程将氧化还原流从NADH转移到NADPH,使滴度提高到52.78 g/L的β-丙氨酸和3.61 g/L的番茄红素。代谢物分析证实SA06中细胞内NADH和FADH水平降低,表明在发酵后期氧化还原平衡得以恢复。发酵过程中的其他改进,包括逐步切换碳源、优化诱导策略以及对生长和生物转化阶段的条件进行微调,使产物滴度进一步提高,达到72 g/L的β-丙氨酸和6.15 g/L的番茄红素。这项研究为微生物联产系统的开发提供了有价值的见解,突出了动态辅因子和氧化还原平衡管理以及过程优化在提高生产效率方面的关键作用。