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L-Lactic Acid Production Using Engineered Saccharomyces cerevisiae with Improved Organic Acid Tolerance.

ABSTRACT: Lactic acid is mainly used to produce bio-based, bio-degradable polylactic acid. For industrial production of lactic acid, engineered Saccharomyces cerevisiae can be used. To avoid cellular toxicity caused by lactic acid accumulation, pH-neutralizing agents are used, leading to increased production costs. In this study, lactic acid-producing S. cerevisiae BK01 was developed with improved lactic acid tolerance through adaptive laboratory evolution (ALE) on 8% lactic acid. The genetic basis of BK01 could not be determined, suggesting complex mechanisms associated with lactic acid tolerance. However, BK01 had distinctive metabolomic traits clearly separated from the parental strain, and lactic acid production was improved by 17% (from 102 g/L to 119 g/L). To the best of our knowledge, this is the highest lactic acid titer produced by engineered S. cerevisiae without the use of pH neutralizers. Moreover, cellulosic lactic acid production by BK01 was demonstrated using acetate-rich buckwheat husk hydrolysates. Particularly, BK01 revealed improved tolerance against acetic acid of the hydrolysates, a major fermentation inhibitor of lignocellulosic biomass. In short, ALE with a high concentration of lactic acid improved lactic acid production as well as acetic acid tolerance of BK01, suggesting a potential for economically viable cellulosic lactic acid production.

SUBMITTER: Jang BK

PROVIDER: S-EPMC8624227 | biostudies-literature | 2021 Oct

REPOSITORIES: biostudies-literature

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l-Lactic Acid Production Using Engineered Saccharomyces cerevisiae with Improved Organic Acid Tolerance.

Jang Byeong-Kwan BK Ju Yebin Y Jeong Deokyeol D Jung Sung-Keun SK Kim Chang-Kil CK Chung Yong-Suk YS Kim Soo-Rin SR

Journal of fungi (Basel, Switzerland) 20211031 11

Lactic acid is mainly used to produce bio-based, bio-degradable polylactic acid. For industrial production of lactic acid, engineered Saccharomyces cerevisiae can be used. To avoid cellular toxicity caused by lactic acid accumulation, pH-neutralizing agents are used, leading to increased production costs. In this study, lactic acid-producing S. cerevisiae BK01 was developed with improved lactic acid tolerance through adaptive laboratory evolution (ALE) on 8% lactic acid. The geneti ...[more]

PMID: 34829217

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Project description:BackgroundSaccharomyces cerevisiae, engineered for L-lactic acid production from glucose and xylose, is a promising production host for lignocellulose-to-lactic acid processes. However, the two principal engineering strategies-pyruvate-to-lactic acid conversion with and without disruption of the competing pyruvate-to-ethanol pathway-have not yet resulted in strains that combine high lactic acid yields (YLA) and productivities (QLA) on both sugar substrates. Limitations seemingly arise from a dependency on the carbon source and the aeration conditions, but the underlying effects are poorly understood. We have recently presented two xylose-to-lactic acid converting strains, IBB14LA1 and IBB14LA1_5, which have the L-lactic acid dehydrogenase from Plasmodium falciparum (pfLDH) integrated at the pdc1 (pyruvate decarboxylase) locus. IBB14LA1_5 additionally has its pdc5 gene knocked out. In this study, the influence of carbon source and oxygen on YLA and QLA in IBB14LA1 and IBB14LA1_5 was investigated.ResultsIn anaerobic fermentation IBB14LA1 showed a higher YLA on xylose (0.27 g g Xyl-1 ) than on glucose (0.18 g g Glc-1 ). The ethanol yields (YEtOH, 0.15 g g Xyl-1 and 0.32 g g Glc-1 ) followed an opposite trend. In IBB14LA1_5, the effect of the carbon source on YLA was less pronounced (~ 0.80 g g Xyl-1 , and 0.67 g g Glc-1 ). Supply of oxygen accelerated glucose conversions significantly in IBB14LA1 (QLA from 0.38 to 0.81 g L-1 h-1) and IBB14LA1_5 (QLA from 0.05 to 1.77 g L-1 h-1) at constant YLA (IBB14LA1 ~ 0.18 g g Glc-1 ; IBB14LA1_5 ~ 0.68 g g Glc-1 ). In aerobic xylose conversions, however, lactic acid production ceased completely in IBB14LA1 and decreased drastically in IBB14LA1_5 (YLA aerobic ≤ 0.25 g g Xyl-1 and anaerobic ~ 0.80 g g Xyl-1 ) at similar QLA (~ 0.04 g L-1 h-1). Switching from aerobic to microaerophilic conditions (pO2 ~ 2%) prevented lactic acid metabolization, observed for fully aerobic conditions, and increased QLA and YLA up to 0.11 g L-1 h-1 and 0.38 g g Xyl-1 , respectively. The pfLDH and PDC activities in IBB14LA1 were measured and shown to change drastically dependent on carbon source and oxygen.ConclusionEvidence from conversion time courses together with results of activity measurements for pfLDH and PDC show that in IBB14LA1 the distribution of fluxes at the pyruvate branching point is carbon source and oxygen dependent. Comparison of the performance of strain IBB14LA1 and IBB14LA1_5 in conversions under different aeration conditions (aerobic, anaerobic, and microaerophilic) further suggest that xylose, unlike glucose, does not repress the respiratory response in both strains. This study proposes new genetic engineering targets for rendering genetically engineering S. cerevisiae better suited for lactic acid biorefineries.

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L-Lactic Acid Production Using Engineered Saccharomyces cerevisiae with Improved Organic Acid Tolerance.

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l-Lactic Acid Production Using Engineered <i>Saccharomyces cerevisiae</i> with Improved Organic Acid Tolerance.

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