Carbon dioxide fixation via production of succinic acid from glycerol in engineered Saccharomyces cerevisiae

Journal Article (2022)
Authors

Zahabiya Malubhoy (Jacobs University Bremen)

Frederico Mendonça Bahia (Università degli Studi di Milano Bicocca, Jacobs University Bremen)

Sophie Claire de Valk (Student TU Delft)

A.F. de Hulster (TU Delft - BT/Industriele Microbiologie)

Toni Rendulić (Jacobs University Bremen)

Juan Paulo Ragas Ortiz (Jacobs University Bremen)

Joeline Xiberras (Jacobs University Bremen)

Mathias Klein (Jacobs University Bremen)

Robert Mans (TU Delft - BT/Industriele Microbiologie)

Elke Nevoigt (Jacobs University Bremen)

Research Group
BT/Industriele Microbiologie
Copyright
© 2022 Zahabiya Malubhoy, Frederico Mendonça Bahia, Sophie Claire de Valk, A.F. de Hulster, Toni Rendulić, Juan Paulo Ragas Ortiz, Joeline Xiberras, Mathias Klein, R. Mans, Elke Nevoigt
To reference this document use:
https://doi.org/10.1186/s12934-022-01817-1
More Info
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Publication Year
2022
Language
English
Copyright
© 2022 Zahabiya Malubhoy, Frederico Mendonça Bahia, Sophie Claire de Valk, A.F. de Hulster, Toni Rendulić, Juan Paulo Ragas Ortiz, Joeline Xiberras, Mathias Klein, R. Mans, Elke Nevoigt
Research Group
BT/Industriele Microbiologie
Issue number
1
Volume number
21
DOI:
https://doi.org/10.1186/s12934-022-01817-1
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Abstract

Background: The microbial production of succinic acid (SA) from renewable carbon sources via the reverse TCA (rTCA) pathway is a process potentially accompanied by net-fixation of carbon dioxide (CO2). Among reduced carbon sources, glycerol is particularly attractive since it allows a nearly twofold higher CO2-fixation yield compared to sugars. Recently, we described an engineered Saccharomyces cerevisiae strain which allowed SA production in synthetic glycerol medium with a maximum yield of 0.23 Cmol Cmol−1. The results of that previous study suggested that the glyoxylate cycle considerably contributed to SA accumulation in the respective strain. The current study aimed at improving the flux into the rTCA pathway accompanied by a higher CO2-fixation and SA yield. Results: By changing the design of the expression cassettes for the rTCA pathway, overexpressing PYC2, and adding CaCO3 to the batch fermentations, an SA yield on glycerol of 0.63 Cmol Cmol−1 was achieved (i.e. 47.1% of the theoretical maximum). The modifications in this 2nd-generation SA producer improved the maximum biomass-specific glycerol consumption rate by a factor of nearly four compared to the isogenic baseline strain solely equipped with the dihydroxyacetone (DHA) pathway for glycerol catabolism. The data also suggest that the glyoxylate cycle did not contribute to the SA production in the new strain. Cultivation conditions which directly or indirectly increased the concentration of bicarbonate, led to an accumulation of malate in addition to the predominant product SA (ca. 0.1 Cmol Cmol−1 at the time point when SA yield was highest). Off-gas analysis in controlled bioreactors with CO2-enriched gas-phase indicated that CO2 was fixed during the SA production phase. Conclusions: The data strongly suggest that a major part of dicarboxylic acids in our 2nd-generation SA-producer was formed via the rTCA pathway enabling a net fixation of CO2. The greatly increased capacity of the rTCA pathway obviously allowed successful competition with other pathways for the common precursor pyruvate. The overexpression of PYC2 and the increased availability of bicarbonate, the co-substrate for the PYC reaction, further strengthened this capacity. The achievements are encouraging to invest in future efforts establishing a process for SA production from (crude) glycerol and CO2.