Choi Sol, Kim Hyun Uk, Kim Tae Yong, Lee Sang Yup
Metabolic and Biomolecular Engineering National Research Laboratory, Department of Chemical and Biomolecular Engineering (BK21 Plus Program), Center for Systems and Synthetic Biotechnology, Institute for the BioCentury, Korea Advanced Institute of Science and Technology (KAIST), Daejeon 34141, Republic of Korea.
Metabolic and Biomolecular Engineering National Research Laboratory, Department of Chemical and Biomolecular Engineering (BK21 Plus Program), Center for Systems and Synthetic Biotechnology, Institute for the BioCentury, Korea Advanced Institute of Science and Technology (KAIST), Daejeon 34141, Republic of Korea; BioInformatics Research Center, KAIST, Daejeon 34141, Republic of Korea.
Metab Eng. 2016 Nov;38:264-273. doi: 10.1016/j.ymben.2016.09.004. Epub 2016 Sep 20.
To address climate change and environmental problems, it is becoming increasingly important to establish biorefineries for the production of chemicals from renewable non-food biomass. Here we report the development of Escherichia coli strains capable of overproducing a four-carbon platform chemical 4-hybroxybutyric acid (4-HB). Because 4-HB production is significantly affected by aeration level, genome-scale metabolic model-based engineering strategies were designed under aerobic and microaerobic conditions with emphasis on oxidative/reductive TCA branches and glyoxylate shunt. Several different metabolic engineering strategies were employed to develop strains suitable for fermentation both under aerobic and microaerobic conditions. It was found that microaerobic condition was more efficient than aerobic condition in achieving higher titer and productivity of 4-HB. The final engineered strain produced 103.4g/L of 4-HB by microaerobic fed-batch fermentation using glycerol. The aeration-dependent optimization strategy of TCA cycle will be useful for developing microbial strains producing other reduced derivative chemicals of TCA cycle intermediates.
为应对气候变化和环境问题,建立用于从可再生非粮生物质生产化学品的生物精炼厂变得越来越重要。在此,我们报告了能够过量生产四碳平台化学品4-羟基丁酸(4-HB)的大肠杆菌菌株的开发情况。由于4-HB的生产受到通气水平的显著影响,基于基因组规模代谢模型的工程策略在有氧和微需氧条件下设计,重点关注氧化/还原TCA分支和乙醛酸循环。采用了几种不同的代谢工程策略来开发适合在有氧和微需氧条件下发酵的菌株。结果发现,在实现更高的4-HB滴度和生产率方面,微需氧条件比有氧条件更有效。最终工程菌株通过使用甘油的微需氧补料分批发酵产生了103.4g/L的4-HB。TCA循环的通气依赖性优化策略将有助于开发生产TCA循环中间体其他还原衍生物化学品的微生物菌株。