4.7 Article

Adaptive laboratory evolution accelerated glutarate production by Corynebacterium glutamicum

Journal

MICROBIAL CELL FACTORIES
Volume 20, Issue 1, Pages -

Publisher

BMC
DOI: 10.1186/s12934-021-01586-3

Keywords

Corynebacterium glutamicum; Glutarate; Adaptive laboratory evolution; Metabolic engineering; Reverse genetics; Volumetric productivity; Reactive extraction

Funding

  1. European Regional Development Fund (ERDF)
  2. Ministry of Economic Affairs, Innovation, Digitalization and Energy of the State of North Rhine-Westphalia by grant Cluster Industrial Biotechnology (CLIB) Kompetenzzentrum Biotechnologie (CKB) [34.EFRE-0300095/1703FI04]
  3. Deutsche Forschungsgemeinschaft
  4. Open Access Publication Fund of Bielefeld University
  5. Projekt DEAL

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Adaptive laboratory evolution was used to improve a C. glutamicum strain engineered for glutarate production by coupling growth to product biosynthesis pathway. The fastest growing mutant showed a twofold higher volumetric productivity compared to the parental strain. Genome sequencing and reverse genetics were used to identify mutations for accelerated glutarate production.
Background The demand for biobased polymers is increasing steadily worldwide. Microbial hosts for production of their monomeric precursors such as glutarate are developed. To meet the market demand, production hosts have to be improved constantly with respect to product titers and yields, but also shortening bioprocess duration is important. Results In this study, adaptive laboratory evolution was used to improve a C. glutamicum strain engineered for production of the C-5-dicarboxylic acid glutarate by flux enforcement. Deletion of the l-glutamic acid dehydrogenase gene gdh coupled growth to glutarate production since two transaminases in the glutarate pathway are crucial for nitrogen assimilation. The hypothesis that strains selected for faster glutarate-coupled growth by adaptive laboratory evolution show improved glutarate production was tested. A serial dilution growth experiment allowed isolating faster growing mutants with growth rates increasing from 0.10 h(-1) by the parental strain to 0.17 h(-1) by the fastest mutant. Indeed, the fastest growing mutant produced glutarate with a twofold higher volumetric productivity of 0.18 g L-1 h(-1) than the parental strain. Genome sequencing of the evolved strain revealed candidate mutations for improved production. Reverse genetic engineering revealed that an amino acid exchange in the large subunit of l-glutamic acid-2-oxoglutarate aminotransferase was causal for accelerated glutarate production and its beneficial effect was dependent on flux enforcement due to deletion of gdh. Performance of the evolved mutant was stable at the 2 L bioreactor-scale operated in batch and fed-batch mode in a mineral salts medium and reached a titer of 22.7 g L-1, a yield of 0.23 g g(-1) and a volumetric productivity of 0.35 g L-1 h(-1). Reactive extraction of glutarate directly from the fermentation broth was optimized leading to yields of 58% and 99% in the reactive extraction and reactive re-extraction step, respectively. The fermentation medium was adapted according to the downstream processing results. Conclusion Flux enforcement to couple growth to operation of a product biosynthesis pathway provides a basis to select strains growing and producing faster by adaptive laboratory evolution. After identifying candidate mutations by genome sequencing causal mutations can be identified by reverse genetics. As exemplified here for glutarate production by C. glutamicum, this approach allowed deducing rational metabolic engineering strategies.

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