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Biocatalytic production of adipic acid from glucose using engineered Saccharomyces cerevisiae.

ABSTRACT: Adipic acid is an important industrial chemical used in the synthesis of nylon-6,6. The commercial synthesis of adipic acid uses petroleum-derived benzene and releases significant quantities of greenhouse gases. Biocatalytic production of adipic acid from renewable feedstocks could potentially reduce the environmental damage and eliminate the need for fossil fuel precursors. Recently, we have demonstrated the first enzymatic hydrogenation of muconic acid to adipic acid using microbial enoate reductases (ERs) - complex iron-sulfur and flavin containing enzymes. In this work, we successfully expressed the Bacillus coagulans ER in a Saccharomyces cerevisiae strain producing muconic acid and developed a three-stage fermentation process enabling the synthesis of adipic acid from glucose. The ability to express active ERs and significant acid tolerance of S. cerevisiae highlight the applicability of the developed yeast strain for the biocatalytic production of adipic acid from renewable feedstocks.

SUBMITTER: Raj K

PROVIDER: S-EPMC5814376 | biostudies-literature | 2018 Jun

REPOSITORIES: biostudies-literature

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Biocatalytic production of adipic acid from glucose using engineered <i>Saccharomyces cerevisiae</i>.

Raj Kaushik K Partow Siavash S Correia Kevin K Khusnutdinova Anna N AN Yakunin Alexander F AF Mahadevan Radhakrishnan R

Metabolic engineering communications 20180203

Adipic acid is an important industrial chemical used in the synthesis of nylon-6,6. The commercial synthesis of adipic acid uses petroleum-derived benzene and releases significant quantities of greenhouse gases. Biocatalytic production of adipic acid from renewable feedstocks could potentially reduce the environmental damage and eliminate the need for fossil fuel precursors. Recently, we have demonstrated the first enzymatic hydrogenation of muconic acid to adipic acid using microbial enoate red ...[more]

PMID: 29487800

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Project description:BACKGROUND:Glycyrrhetinic acid (GA) is the most important ingredient in licorice due to its outstanding anti-inflammatory activity and wide application in the medicine and cosmetics industries. Contemporary industrial production of GA by acid hydrolysis of glycyrrhizin which was extracted from Glycyrrhiza plants, is not environment-friendly and devastates farmland since the Glycyrrhiza rhizomes grow up to 10 m underground. RESULTS:In this study, GA was produced through metabolically engineering Saccharomyces cerevisiae by introducing the entire heterogeneous biosynthetic pathway of GA. Codon optimized CYP88D6 and CYP72A154, combined with ?-AS (?-amyrin synthase encoding gene) and the NADPH-cytochrome P450 reductase gene of Arabidopsis thaliana were introduced into S. cerevisiae. The resulting strain (Y1) produced 2.5 mg/L of ?-amyrin and 14 ?g/L of GA. The cytochrome b5 from G. uralensis (GuCYB5) was identified and the introduction of this novel GuCYB5 increased the efficiency of GA production by eightfold. The joint utilization of the GuCYB5 gene along with 10 known MVA pathway genes from S. cerevisiae were overexpressed in a stable chromosome integration to achieve higher GA production. Using the combined strategy, GA concentration improved by 40-fold during batch fermentation. The production was further improved to 8.78 mg/L in fed-batch fermentation, which was increased by a factor of nearly 630. CONCLUSIONS:This study first investigated the influence of carbon flux in the upstream module and the introduction of a newly identified GuCYB5 on GA production. The newly identified GuCYB5 was highly effective in improving GA production. An integrated strategy including enzyme discovery, pathway optimization, and fusion protein construction was provided in improving GA production, achieving a 630 fold increase in GA production. The metabolically engineered yeast cell factories provide an alternative approach to glycyrrhetinic acid production, replacing the traditional method of plant extraction.

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.

Dataset Information

Biocatalytic production of adipic acid from glucose using engineered Saccharomyces cerevisiae.

Publications

Biocatalytic production of adipic acid from glucose using engineered <i>Saccharomyces cerevisiae</i>.

Similar Datasets

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