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Increased CO 2 fixation enables high carbon-yield production of 3-hydroxypropionic acid in yeast

Qin, Ning (author)
Beijing University of Chemical Technology
Li, Lingyun (author)
Beijing University of Chemical Technology
Wan, Xiaozhen (author)
Beijing University of Chemical Technology
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Ji, Xu (author)
Beijing University of Chemical Technology
Chen, Yu, 1990 (author)
Shenzhen Institute of Advanced Technology
Li, Chaokun (author)
Helsingin Yliopisto,University of Helsinki
Liu, Ping (author)
Beijing University of Chemical Technology
Zhang, Yijie (author)
Beijing University of Chemical Technology
Yang, Weijie (author)
Beijing University of Chemical Technology
Jiang, Junfeng (author)
Xia, Jianye (author)
Shi, Shuobo, 1981 (author)
Beijing University of Chemical Technology
Tan, Tianwei (author)
Beijing University of Chemical Technology
Nielsen, Jens B, 1962 (author)
Beijing University of Chemical Technology,Chalmers tekniska högskola,Chalmers University of Technology,BioInnovation Institute (BII)
Chen, Yun, 1978 (author)
Chalmers tekniska högskola,Chalmers University of Technology,Novo Nordisk Fonden,Novo Nordisk Foundation
Liu, Zihe, 1984 (author)
Beijing University of Chemical Technology
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 (creator_code:org_t)
2024
2024
English.
In: Nature Communications. - 2041-1723 .- 2041-1723. ; 15:1
  • Journal article (peer-reviewed)
Abstract Subject headings
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  • CO2 fixation plays a key role to make biobased production cost competitive. Here, we use 3-hydroxypropionic acid (3-HP) to showcase how CO2 fixation enables approaching theoretical-yield production. Using genome-scale metabolic models to calculate the production envelope, we demonstrate that the provision of bicarbonate, formed from CO2, restricts previous attempts for high yield production of 3-HP. We thus develop multiple strategies for bicarbonate uptake, including the identification of Sul1 as a potential bicarbonate transporter, domain swapping of malonyl-CoA reductase, identification of Esbp6 as a potential 3-HP exporter, and deletion of Uga1 to prevent 3-HP degradation. The combined rational engineering increases 3-HP production from 0.14 g/L to 11.25 g/L in shake flask using 20 g/L glucose, approaching the maximum theoretical yield with concurrent biomass formation. The engineered yeast forms the basis for commercialization of bio-acrylic acid, while our CO2 fixation strategies pave the way for CO2 being used as the sole carbon source.

Subject headings

TEKNIK OCH TEKNOLOGIER  -- Kemiteknik -- Kemiska processer (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Chemical Engineering -- Chemical Process Engineering (hsv//eng)
TEKNIK OCH TEKNOLOGIER  -- Industriell bioteknik -- Bioprocessteknik (hsv//swe)
ENGINEERING AND TECHNOLOGY  -- Industrial Biotechnology -- Bioprocess Technology (hsv//eng)

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