Improved fermentative production of the compatible solute ectoine by Corynebacterium glutamicum from glucose and alternative carbon sources.

The cyclic amino acid ectoine is a compatible solute serving as a protective substance against osmotic stress. Ectoine finds various applications due to its moisturizing effect. To avoid the disadvantages of the prevailing so-called "bacterial milking ectoine production process" caused by the high salt concentration, low salt fermentation strategies are sought after. As l-lysine and ectoine biosynthesis share l-aspartate-semialdehyde as common precursor, l-lysine producing strains can be converted to ectoine producing strains. Corynebacterium glutamicum, which is used for l-lysine production in the million-ton-scale, was engineered for ectoine production by heterologous expression of the ectoine biosynthesis operon ectABC from Chromohalobacter salexigens. Derepression of glucose metabolism by deletion of the regulatory gene sugR and avoiding l-lactate formation by deletion of the lactate dehydrogenase gene ldhA increased ectoine productivity. In bioreactor fed-batch cultivations an ectoine titer of 22gL-1 and a volumetric productivity of 0.32gL-1h-1 were obtained. The ectoine yield of 0.16gg-1, to the best of our knowledge, exceeded previously reported yields. Moreover, ectoine production from the alternative carbon sources glycerol, glucosamine, xylose, arabinose, and soluble starch was achieved.

Corynebacterium glutamicum tailored for efficient isobutanol production.

We recently engineered Corynebacterium glutamicum for aerobic production of 2-ketoisovalerate by inactivation of the pyruvate dehydrogenase complex, pyruvate:quinone oxidoreductase, transaminase B, and additional overexpression of the ilvBNCD genes, encoding acetohydroxyacid synthase, acetohydroxyacid isomeroreductase, and dihydroxyacid dehydratase. Based on this strain, we engineered C. glutamicum for the production of isobutanol from glucose under oxygen deprivation conditions by inactivation of l-lactate and malate dehydrogenases, implementation of ketoacid decarboxylase from Lactococcus lactis, alcohol dehydrogenase 2 (ADH2) from Saccharomyces cerevisiae, and expression of the pntAB transhydrogenase genes from Escherichia coli. The resulting strain produced isobutanol with a substrate-specific yield (Y(P/S)) of 0.60 ± 0.02 mol per mol of glucose. Interestingly, a chromosomally encoded alcohol dehydrogenase rather than the plasmid-encoded ADH2 from S. cerevisiae was involved in isobutanol formation with C. glutamicum, and overexpression of the corresponding adhA gene increased the Y(P/S) to 0.77 ± 0.01 mol of isobutanol per mol of glucose. Inactivation of the malic enzyme significantly reduced the Y(P/S), indicating that the metabolic cycle consisting of pyruvate and/or phosphoenolpyruvate carboxylase, malate dehydrogenase, and malic enzyme is responsible for the conversion of NADH + H+ to NADPH + H+. In fed-batch fermentations with an aerobic growth phase and an oxygen-depleted production phase, the most promising strain, C. glutamicum ΔaceE Δpqo ΔilvE ΔldhA Δmdh(pJC4ilvBNCD-pntAB)(pBB1kivd-adhA), produced about 175 mM isobutanol, with a volumetric productivity of 4.4 mM h⁻¹, and showed an overall Y(P/S) of about 0.48 mol per mol of glucose in the production phase.