Engineering Escherichia coli for high-titer de novo biosynthesis of the N-nucleoside antibiotic Angustmycin A

Abstract Background Angustmycin A (also known as guvermectin) is a rare N-nucleoside antibiotic with broad-spectrum antimicrobial activity and registered agricultural use as a plant growth-promoting biochemical pesticide. Native Streptomyces producers remain the primary production source, but their slow growth, long fermentation cycles, and limited genetic tractability constrain both titer improvement and process development. Establishing a fast-growing, genetically flexible host for de novo Angustmycin A biosynthesis from glucose is therefore a practical priority. Results An Escherichia coli ( E. coli ) microbial cell factory was constructed for de novo Angustmycin A biosynthesis through four sequential engineering stages. First, consolidation of the six-enzyme pathway onto a single medium-copy plasmid and deletion of pfkA to redirect fructose-6-phosphate (F6P) flux increased production from 142 mg L − 1 to 649 ± 9.0 mg L − 1 . Second, pathway bottleneck analysis identified AgmC solubility as a primary constraint; AgmC-centered liquid–liquid phase separation (LLPS) recruitment, combined with co-recruitment of AgmA, relieved this bottleneck and improved production to 699 ± 7.2 mg L − 1 . Third, orthogonal optimization of cultivation parameters and chromosomal gltA 5′-UTR engineering to moderate TCA cycle flux further increased shake-flask production to 1225 ± 12.9 mg L − 1 . Finally, fed-batch fermentation of the final strain in a 1.2-L bioreactor produced 1805 ± 74.1 mg L − 1 Angustmycin A at 96 h (volumetric productivity: ~18.8 mg L −1 h − 1 ). Conclusions This work establishes a high-performing E. coli cell factory for gram-per-liter de novo production of Angustmycin A from glucose. The engineered strain reached 1.805 g L − 1 within 96 h and a maximum titer of approximately 1.92 g L − 1 during extended fed-batch cultivation, demonstrating rapid product accumulation while achieving the highest reported Angustmycin A titer to date. F6P flux rewiring and mitigation of limited soluble AgmC availability emerged as two major engineering levers for improving pathway performance. More broadly, the integrated strategy of precursor-flux redistribution and bottleneck-guided enzyme recruitment provides a transferable framework for microbial production of related N-nucleoside natural products.

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Journal
Microbial Cell Factories
Published
2026-10-13
DOI
https://doi.org/10.1186/s12934-026-03136-1
Primary Topic
Microbial Metabolic Engineering and Bioproduction
Type
article
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article

Engineering Escherichia coli for high-titer de novo biosynthesis of the N-nucleoside antibiotic Angustmycin A

HE Haibing, Shumin Lin, Biming Zhong, Xinran Wang et al.
Microbial Cell Factories
Microbial Metabolic Engineering and Bioproduction
article

Engineering Escherichia coli for high-titer de novo biosynthesis of the N-nucleoside antibiotic Angustmycin A

HE Haibing, Shumin Lin, Biming Zhong, Xinran Wang, Xiaozhou Luo, Yuele Teng, Yulan Qiu
article en

Abstract

Abstract Background Angustmycin A (also known as guvermectin) is a rare N-nucleoside antibiotic with broad-spectrum antimicrobial activity and registered agricultural use as a plant growth-promoting biochemical pesticide. Native Streptomyces producers remain the primary production source, but their slow growth, long fermentation cycles, and limited genetic tractability constrain both titer improvement and process development. Establishing a fast-growing, genetically flexible host for de novo Angustmycin A biosynthesis from glucose is therefore a practical priority. Results An Escherichia coli ( E. coli ) microbial cell factory was constructed for de novo Angustmycin A biosynthesis through four sequential engineering stages. First, consolidation of the six-enzyme pathway onto a single medium-copy plasmid and deletion of pfkA to redirect fructose-6-phosphate (F6P) flux increased production from 142 mg L − 1 to 649 ± 9.0 mg L − 1 . Second, pathway bottleneck analysis identified AgmC solubility as a primary constraint; AgmC-centered liquid–liquid phase separation (LLPS) recruitment, combined with co-recruitment of AgmA, relieved this bottleneck and improved production to 699 ± 7.2 mg L − 1 . Third, orthogonal optimization of cultivation parameters and chromosomal gltA 5′-UTR engineering to moderate TCA cycle flux further increased shake-flask production to 1225 ± 12.9 mg L − 1 . Finally, fed-batch fermentation of the final strain in a 1.2-L bioreactor produced 1805 ± 74.1 mg L − 1 Angustmycin A at 96 h (volumetric productivity: ~18.8 mg L −1 h − 1 ). Conclusions This work establishes a high-performing E. coli cell factory for gram-per-liter de novo production of Angustmycin A from glucose. The engineered strain reached 1.805 g L − 1 within 96 h and a maximum titer of approximately 1.92 g L − 1 during extended fed-batch cultivation, demonstrating rapid product accumulation while achieving the highest reported Angustmycin A titer to date. F6P flux rewiring and mitigation of limited soluble AgmC availability emerged as two major engineering levers for improving pathway performance. More broadly, the integrated strategy of precursor-flux redistribution and bottleneck-guided enzyme recruitment provides a transferable framework for microbial production of related N-nucleoside natural products.

Microbial Cell Factories
Hong Kong Polytechnic University (HK), Chinese Academy of Sciences (CN), Shenzhen Institutes of Advanced Technology (CN), University of Chinese Academy of Sciences (CN), Shenzhen Institute of Synthetic Biology (CN)
National Natural Science Foundation of China, National Key Research and Development Program of China, Science and Technology Planning Project of Guangdong Province, Shenzhen Science and Technology Innovation Program, Basic and Applied Basic Research Foundation of Guangdong Province
Openalex Percentile: Top 24%
Microbial Metabolic Engineering and Bioproduction
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