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通过代谢工程提高乙酸盐生产二醇的能力。

Metabolic Engineering of for Enhanced Diols Production from Acetate.

作者信息

Ricci Luca, Cen Xuecong, Zu Yuexuan, Antonicelli Giacomo, Chen Zhen, Fino Debora, Pirri Fabrizio C, Stephanopoulos Gregory, Woolston Benjamin M, Re Angela

机构信息

Department of Chemical Engineering, Massachusetts Institute of Technology, Cambridge, Massachusetts 02142, United States.

Centre for Sustainable Future Technologies, Fondazione Istituto Italiano di Tecnologia, Via Livorno 60, 10144 Turin, Italy.

出版信息

ACS Synth Biol. 2025 Apr 18;14(4):1204-1219. doi: 10.1021/acssynbio.4c00839. Epub 2025 Mar 18.

Abstract

Effective employment of renewable carbon sources is highly demanded to develop sustainable biobased manufacturing. Here, we developed strains to produce 2,3-butanediol and acetoin (collectively referred to as diols) using acetate as the sole carbon source by stepwise metabolic engineering. When tested in fed-batch experiments, the strain overexpressing the entire acetate utilization pathway was found to consume acetate at a 15% faster rate (0.78 ± 0.05 g/g/h) and to produce a 35% higher diol titer (1.16 ± 0.01 g/L) than the baseline diols-producing strain. Moreover, singularly overexpressing the genes encoding alternative acetate uptake pathways as well as alternative isoforms of genes in the malate-to-pyruvate pathway unveiled that leveraging and is more effective in enhancing acetate consumption and diols production, compared to and . Finally, the increased substrate consumption rate and diol production obtained in flask-based experiments were confirmed in bench-scale bioreactors operated in fed-batch mode. Consequently, the highest titer of 1.56 g/L achieved in this configuration increased by over 30% compared to the only other similar effort carried out so far.

摘要

为了发展可持续的生物基制造业,人们对有效利用可再生碳源有很高的需求。在此,我们通过逐步代谢工程开发了利用乙酸盐作为唯一碳源生产2,3-丁二醇和乙偶姻(统称为二醇)的菌株。在分批补料实验中测试时,发现过表达整个乙酸盐利用途径的菌株消耗乙酸盐的速度比基线二醇生产菌株快15%(0.78±0.05 g/g/h),二醇产量高35%(1.16±0.01 g/L)。此外,单独过表达编码替代乙酸盐摄取途径的基因以及苹果酸到丙酮酸途径中基因的替代同工型发现,与[具体内容缺失]相比,利用[具体内容缺失]在提高乙酸盐消耗和二醇生产方面更有效。最后,在分批补料模式运行的实验室规模生物反应器中证实了在基于摇瓶的实验中获得的增加的底物消耗速率和二醇产量。因此,与迄今为止进行的唯一其他类似工作相比,这种配置下实现的最高滴度1.56 g/L提高了30%以上。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/0fc5/12012870/0588519f04cc/sb4c00839_0001.jpg

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