Microaerobic growth‐decoupled production of α‐ketoglutarate and succinate from xylose in a one‐pot process using Corynebacterium glutamicum

谷氨酸棒杆菌 木糖 化学 代谢工程 生物化学 原材料 发酵 有机化学 基因
作者
Niklas Tenhaef,Jannick Kappelmann,Arabel Eich,Marc Weiske,Lisette Brieß,Christian Brüsseler,Jan Marienhagen,Wolfgang Wiechert,Stephan Noack
出处
期刊:Biotechnology Journal [Wiley]
卷期号:16 (9) 被引量:15
标识
DOI:10.1002/biot.202100043
摘要

Abstract Background Lignocellulosic biomass is the most abundant raw material on earth. Its efficient use for novel bio‐based materials is essential for an emerging bioeconomy. Possible building blocks for such materials are the key TCA‐cycle intermediates α‐ketoglutarate and succinate. These organic acids have a wide range of potential applications, particularly in use as monomers for established or novel biopolymers. Recently, Corynebacterium glutamicum was successfully engineered and evolved towards an improved utilization of d ‐xylose via the Weimberg pathway, yielding the strain WMB2 evo . The Weimberg pathway enables a carbon‐efficient C5‐to‐C5 conversion of d ‐xylose to α‐ketoglutarate and a shortcut route to succinate as co‐product in a one‐pot process. Methods and Results C. glutamicum WMB2 evo was grown under dynamic microaerobic conditions on d ‐xylose, leading to the formation of comparably high amounts of succinate and only small amounts of α‐ketoglutarate. Subsequent carbon isotope labeling experiments verified the targeted production route for both products in C. glutamicum WMB2 evo . Fed‐batch process development was initiated and the effect of oxygen supply and feeding strategy for a growth‐decoupled co‐production of α‐ketoglutarate and succinate were studied in detail. The finally established fed‐batch production process resulted in the formation of 78.4 mmol L −1 (11.45 g L −1 ) α‐ketoglutarate and 96.2 mmol L −1 (11.36 g L −1 ) succinate. Conclusion The developed one‐pot process represents a promising approach for the combined supply of bio‐based α‐ketoglutarate and succinate. Future work will focus on tailor‐made down‐stream processing of both organic acids from the fermentation broth to enable their application as building blocks in chemical syntheses. Alternatively, direct conversion of one or both acids via whole‐cell or cell‐free enzymatic approaches can be envisioned; thus, extending the network of value chains starting from cheap and renewable d ‐xylose.
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