Department of Chemical Engineering and Applied Chemistry, University of Toronto, 200 College Street, Toronto, ON, M5S 3E5, Canada.
Institute of Biomedical Engineering, University of Toronto, 164 College Street, Toronto, ON, M5S 3G9, Canada.
Microb Cell Fact. 2021 Jan 22;20(1):22. doi: 10.1186/s12934-021-01509-2.
A considerable challenge in the development of bioprocesses for producing chemicals and fuels has been the high cost of feedstocks relative to oil prices, making it difficult for these processes to compete with their conventional petrochemical counterparts. Hence, in the absence of high oil prices in the near future, there has been a shift in the industry to produce higher value compounds such as fragrances for cosmetics. Yet, there is still a need to address climate change and develop biotechnological approaches for producing large market, lower value chemicals and fuels.
In this work, we study ethylene glycol (EG), a novel feedstock that we believe has promise to address this challenge. We engineer Escherichia coli (E. coli) to consume EG and examine glycolate production as a case study for chemical production. Using a combination of modeling and experimental studies, we identify oxygen concentration as an important metabolic valve in the assimilation and use of EG as a substrate. Two oxygen-based strategies are thus developed and tested in fed-batch bioreactors. Ultimately, the best glycolate production strategy employed a target respiratory quotient leading to the highest observed fermentation performance. With this strategy, a glycolate titer of 10.4 g/L was reached after 112 h of production time in a fed-batch bioreactor. Correspondingly, a yield of 0.8 g/g from EG and productivity of 0.1 g/L h were measured during the production stage. Our modeling and experimental results clearly suggest that oxygen concentration is an important factor in the assimilation and use of EG as a substrate. Finally, our use of metabolic modeling also sheds light on the intracellular distribution through central metabolism, implicating flux to 2-phosphoglycerate as the primary route for EG assimilation.
Overall, our work suggests that EG could provide a renewable starting material for commercial biosynthesis of fuels and chemicals that may achieve economic parity with petrochemical feedstocks while sequestering carbon dioxide.
在开发生产化学品和燃料的生物工艺方面,一个相当大的挑战是相对于石油价格而言,原料成本较高,使得这些工艺难以与传统的石油化工工艺竞争。因此,在近期内没有高油价的情况下,该行业已转向生产附加值更高的化合物,如化妆品用香料。然而,仍然需要解决气候变化问题,并开发生产大型市场、低价值化学品和燃料的生物技术方法。
在这项工作中,我们研究了乙二醇(EG),这是一种新型原料,我们相信它有希望解决这一挑战。我们通过工程改造大肠杆菌(E. coli)来消耗 EG,并将其作为生产化学物质的案例研究来研究甘醇酸盐的生产。我们使用建模和实验研究的组合,确定氧浓度是同化和利用 EG 作为底物的重要代谢阀。因此,开发并测试了两种基于氧的策略。最终,最佳的甘醇酸盐生产策略采用了目标呼吸商,从而实现了最高的发酵性能。采用该策略,在分批补料生物反应器中经过 112 小时的生产时间,达到了 10.4 g/L 的甘醇酸盐滴度。相应地,从 EG 获得了 0.8 g/g 的产率和 0.1 g/L·h 的生产率。我们的建模和实验结果清楚地表明,氧浓度是同化和利用 EG 作为底物的一个重要因素。最后,我们使用代谢建模也揭示了通过中心代谢的细胞内分布,表明 EG 同化的主要途径是流向 2-磷酸甘油酸。
总的来说,我们的工作表明,EG 可以为商业生物合成燃料和化学品提供可再生的起始原料,这些原料可能在与石油化工原料达到经济平价的同时,还能固定二氧化碳。