Cha Seungwoo, Jo Jae-Hwan, Lee Jong Kwan, Park Wooyoung, Moon Myounghoon, Park Gwon Woo, Kim Min-Sik, Hahn Ji-Sook
Department of Chemical and Biological Engineering, Institute of Chemical Processes, Seoul National University, 1 Gwanak-Ro, Gwanak-Gu, Seoul, 08826, Republic of Korea.
Bioenergy and Resources Upcycling Research Laboratory, Korea Institute of Energy Research, 152 Gajeong-Ro, Yuseong-Gu, Daejeon, 34129, Republic of Korea.
Microb Cell Fact. 2025 Mar 25;24(1):70. doi: 10.1186/s12934-025-02695-z.
Methane is an abundant and low-cost carbon source with great potential for conversion into value-added chemicals. Methanotrophs, microorganisms that utilize methane as their sole carbon and energy source, present a promising platform for biotechnological applications. This study aimed to engineer Methylomonas sp. DH-1 to enhance D-LA production through metabolic pathway optimization during large-scale cultivation.
In this study, we regulated the expression of D-lactate dehydrogenase (D-LDH) using a Ptac promoter with IPTG induction to mitigate the toxic effects of lactate accumulation. To further optimize carbon flow away from glycogen, the glgA gene was deleted. However, this modification led to growth inhibition, especially during scale-up, likely due to the accumulation of ADP-glucose caused by the rewired carbon flux under carbon-excess conditions. Deleting the glgC gene, which encodes glucose 1-phosphate adenylyltransferase, alleviated this issue. The final optimized strain, JHM805, achieved a D-LA production of 6.17 g/L in a 5-L bioreactor, with a productivity of 0.057 g/L/h, marking a significant improvement in D-LA production from methane.
The metabolic engineering strategies employed in this study, including the use of an inducible promoter and alleviation of ADP-glucose accumulation toxicity, successfully enhanced the ability of the strain to produce D-LA from methane. Furthermore, optimizing the bioreactor fermentation process through methane and nitrate supplementation resulted in a significant increase in both the titer and productivity, exceeding previously reported values.
甲烷是一种丰富且低成本的碳源,具有转化为高附加值化学品的巨大潜力。甲烷氧化菌是一类以甲烷作为唯一碳源和能源的微生物,为生物技术应用提供了一个有前景的平台。本研究旨在对甲基单胞菌属DH-1进行工程改造,以通过大规模培养过程中的代谢途径优化来提高D-乳酸的产量。
在本研究中,我们使用Ptac启动子并通过IPTG诱导来调节D-乳酸脱氢酶(D-LDH)的表达,以减轻乳酸积累的毒性作用。为了进一步优化碳流使其远离糖原,删除了glgA基因。然而,这种修饰导致生长抑制,尤其是在放大培养过程中,这可能是由于在碳过量条件下重新布线的碳通量导致ADP-葡萄糖积累所致。删除编码葡萄糖1-磷酸腺苷酰转移酶的glgC基因缓解了这个问题。最终优化的菌株JHM805在5-L生物反应器中实现了6.17 g/L的D-乳酸产量,生产率为0.057 g/L/h,标志着从甲烷生产D-乳酸有了显著提高。
本研究中采用的代谢工程策略,包括使用诱导型启动子和减轻ADP-葡萄糖积累毒性,成功提高了菌株从甲烷生产D-乳酸的能力。此外,通过补充甲烷和硝酸盐优化生物反应器发酵过程,使产量和生产率都显著提高,超过了先前报道的值。