Metabolic engineering of Corynebacterium glutamicum for the production of 3-hydroxypropionic acid from glucose and xylose

3-Hydroxypropionic acid (3-HP) is a promising platform chemical which can be used for the production of various value-added chemicals. In this study,Corynebacterium glutamicum was metabolically engineered to efficiently produce 3-HP from glucose and xylose via the glycerol pathway. A functional 3-HP synthesis pathway was engineered through a combination of genes involved in glycerol synthesis (fusion of gpd and gpp from Saccharomyces cerevisiae) and 3-HP production (pduCDEGH from Klebsiella pneumoniae and aldehyde dehydrogenases from various resources). High 3-HP yield was achieved by screening of active aldehyde dehydrogenases and by minimizing byproduct synthesis (gapA^A1GΔldhAΔpta-ackAΔpoxBΔglpK). Substitution of phosphoenolpyruvate-dependent glucose uptake system (PTS) by inositol permeases (iolT1) and glucokinase (glk) further increased 3-HP production to 38.6 g/L, with the yield of 0.48 g/g glucose. To broaden its substrate spectrum, the engineered strain was modified to incorporate the pentose transport gene araE and xylose catabolic gene xylAB, allowing for the simultaneous utilization of glucose and xylose. Combination of these genetic manipulations resulted in an engineered C. glutamicum strain capable of producing 62.6 g/L 3-HP at a yield of 0.51 g/g glucose in fed-batch fermentation. To the best of our knowledge, this is the highest titer and yield of 3-HP from sugar. This is also the first report for the production of 3-HP from xylose, opening the way toward 3-HP production from abundant lignocellulosic feedstocks.     

Ala258Phe substitution in Bacillus sp. YX-1 glucose dehydrogenase improves its substrate preference for xylose

Bacillus sp. YX-1 glucose dehydrogenase (BsGDH) with good solvent resistance catalyzes the oxidation of β-d-glucose to d-glucono-1,5-lactone. Xylose is a recyclable resource from hemicellulase hydrolysis. In this work, to improve the preference of BsGDH for xylose, we designed seven mutants inside or adjacent to the substrate binding pocket using site-directed mutagenesis. Among all mutants, Ala258Phe mutant displayed the highest activity of 7.59 U mg⁻¹ and nearly 8-folds higher k_cat/K_m value towards xylose than wild-type BsGDH. The kinetic constants indicated that the A258F mutation effectively altered the transition state. By analysis of modeled protein structure, Ala258Phe created a space to facilitate the reactivity towards xylose. A258F mutant retained good solvent resistance in glycol, ethyl caprylate, octane, decane, cyclohexane, nonane, etc. as with BsGDH. This work provides a protein engineering approach to modify the substrate stereo-preference of alcohol dehydrogenase and a promising enzyme for cofactor regeneration in chiral catalysis.     

Metabolic engineering of Cupriavidus necator for heterotrophic and autotrophic alka(e)ne production

Alkanes of defined carbon chain lengths can serve as alternatives to petroleum-based fuels. Recently, microbial pathways of alkane biosynthesis have been identified and enabled the production of alkanes in non-native producing microorganisms using metabolic engineering strategies. The chemoautotrophic bacterium Cupriavidus necator has great potential for producing chemicals from CO₂: it is known to have one of the highest growth rate among natural autotrophic bacteria and under nutrient imbalance it directs most of its carbon flux to the synthesis of the acetyl-CoA derived polymer, polyhydroxybutyrate (PHB), (up to 80% of intracellular content). Alkane synthesis pathway from Synechococcus elongatus (2 genes coding an acyl-ACP reductase and an aldehyde deformylating oxygenase) was heterologously expressed in a C. necator mutant strain deficient in the PHB synthesis pathway. Under heterotrophic condition on fructose we showed that under nitrogen limitation, in presence of an organic phase (decane), the strain produced up to 670 mg/L total hydrocarbons containing 435 mg/l of alkanes consisting of 286 mg/l of pentadecane, 131 mg/l of heptadecene, 18 mg/l of heptadecane, and 236 mg/l of hexadecanal. We report here the highest level of alka(e)nes production by an engineered C. necator to date. We also demonstrated the first reported alka(e)nes production by a non-native alkane producer from CO₂ as the sole carbon source.     

Dihydroxyacetone production in an engineered Escherichia coli through expression of Corynebacterium glutamicum dihydroxyacetone phosphate dephosphorylase

Dihydroxyacetone (DHA) has several industrial applications such as a tanning agent in tanning lotions in the cosmetic industry; its production via microbial fermentation would present a more sustainable option for the future. Here we genetically engineered Escherichia coli (E. coli) for DHA production from glucose. Deletion of E. coli triose phosphate isomerase (tpiA) gene was carried out to accumulate dihydroxyacetone phosphate (DHAP), for use as the main intermediate or precursor for DHA production. The accumulated DHAP was then converted to DHA through the heterologous expression of Corynebacterium glutamicum DHAP dephosphorylase (cghdpA) gene. To conserve DHAP exclusively for DHA production we removed methylglyoxal synthase (mgsA) gene in the ΔtpiA strain. This drastically improved DHA production from 0.83 g/l (0.06 g DHA/g glucose) in the ΔtpiA strain bearing cghdpA to 5.84 g/l (0.41 g DHA/g glucose) in the ΔtpiAΔmgsA double mutant containing the same gene. To limit the conversion of intracellular DHA to glycerol, glycerol dehydrogenase (gldA) gene was further knocked out resulting in a ΔtpiAΔmgsAΔgldA triple mutant. This triple mutant expressing the cghdpA gene produced 6.60 g/l of DHA at 87% of the maximum theoretical yield. In summary, we demonstrated an efficient system for DHA production in genetically engineered E. coli strain.     

Deciphering and engineering of the final step halogenase for improved chlortetracycline biosynthesis in industrial Streptomyces aureofaciens

Chlortetracycline (CTC) is an important member from antibiotics tetracycline (TC) family, which inhibits protein synthesis in bacteria and is widely involved in clinical therapy, animal feeds and aquaculture. Previous works have reported intricately the biosynthesis of CTC from the intermediates in random mutants of Streptomyces aureofaciens and the crucial chlorination remained unclear. We have developed the genetic manipulation in an industrial producer, in which about 15.0 g/l CTC predominated along with 1.2 g/l TC, and discovered that chlorination by ctcP (an FADH₂-dependent halogenase gene) is the last inefficient step during CTC biosynthesis. Firstly, the ΔctcP strain accumulated about 18.9 g/l “clean” TC without KBr addition and abolished the production of CTC. Subsequently, CtcP was identified to exhibit a substrate stereo-specificity to absolute TC (4S) rather than TC (4R), with low k_cat of 0.51±0.01 min⁻¹, while it could halogenate several TC analogs. Accordingly, we devised a strategy for overexpression of ctcP in S. aureofaciens and improved CTC production to a final titer of 25.9 g/l. We anticipate that our work will provide a biotechnological potential of enzymatic evolution and strain engineering towards new TC derivatives in microorganisms.     

Unmarked insertional inactivation in the gfo gene improves growth and ethanol production by Zymomonas mobilis ZM4 in sucrose without formation of sorbitol as a by-product,but yields opposite effects in high glucose

Sorbitol, one of the main by-products of growth on high sucrose concentrations, is catalyzed by glucose-fructose oxidoreductase (GFOR, EC 1.1.99.28) in Zymomonas mobilis, which decreases the ethanol yield. In this study, an unmarked gfo mutant from Z. mobilis ZM4 was constructed using a site-specific FLP recombinase, and growth and ethanol production were evaluated with or without the addition of sorbitol to the media. The inactivation of gfo had contrasting effects in different substrates, especially at high concentrations. The maximum specific growth rate (μ_m) and theoretical ethanol yield value (Y_m) increased from 0.065 h⁻¹ and 60.56% to 0.094 h⁻¹ and 83.87% in 342 g/L sucrose, respectively. Conversely, in 200 g/L glucose, gfo inactivation decreased μ_m and Y_m from 0.15 h⁻¹ and 89.85% to 0.10 h⁻¹ and 67.59%, respectively, and prolonged the lag period from 16 h to 40 h. The addition of sorbitol slightly accelerated growth and sucrose hydrolysis by the gfo mutant in 342 g/L sucrose; however, addition of sorbitol restored the μ_m and Y_m of the gfo mutant in 200 g/L glucose to 0.14 h⁻¹ and 82.50%, respectively. Inactivation of gfo had a small effect on fructose utilization, and a positive one on mixture of glucose and fructose similar to that on sucrose. These results provide further understanding of the osmoregulation mechanisms in Z. mobilis and may help to exploit the biotechnological applications of this industrially important bacterium.     

Combining metabolic engineering and biocompatible chemistry for high-yield production of homo-diacetyl and homo-(S,S)-2,3-butanediol

Biocompatible chemistry is gaining increasing attention because of its potential within biotechnology for expanding the repertoire of biological transformations carried out by enzymes. Here we demonstrate how biocompatible chemistry can be used for synthesizing valuable compounds as well as for linking metabolic pathways to achieve redox balance and rescued growth. By comprehensive rerouting of metabolism, activation of respiration, and finally metal ion catalysis, we successfully managed to convert the homolactic bacterium Lactococcus lactis into a homo-diacetyl producer with high titer (95 mM or 8.2 g/L) and high yield (87% of the theoretical maximum). Subsequently, the pathway was extended to (S,S)-2,3-butanediol (S-BDO) through efficiently linking two metabolic pathways via chemical catalysis. This resulted in efficient homo-S-BDO production with a titer of 74 mM (6.7 g/L) S-BDO and a yield of 82%. The diacetyl and S-BDO production rates and yields obtained are the highest ever reported, demonstrating the promising combination of metabolic engineering and biocompatible chemistry as well as the great potential of L. lactis as a new production platform.     

Genomic engineering of Escherichia coli by the phage attachment site-based integration system with mutant loxP sites

Metabolic engineering of Escherichia coli using plasmids is problematic, which is addressed by developing a toolbox for genomic engineering of E. coli. This toolbox includes the attP site-based integration vectors and the attB site-based template vectors, equipped with mutant loxP sites (i.e., LE* and RE*). The former vectors facilitate integration of passenger genes into attB sites while the latter allows creation of new attB sites. Consequently, the inserted vector backbone is flanked by LE* and RE* sites and can be rescued by Cre. Based on this approach, the biosynthetic pathway of poly(3-hydroxybutyric acid) was first built in E. coli. By scoring the observable phenotype of integrants, the result revealed that the efficiency of gene integration could reach 100%. In addition, reconstruction of the n-butanol-synthesizing pathway in E. coli resulted in a plasmid-free producer strain. As a consequence, the producer strain was able to stably overproduce n-butanol (3.7 g/L) from glucose (20 g/L). Finally, exoglucanase was overexpressed in E. coli that carried multiple genomic copies of the celY gene. Overall, it indicates a promise of our method for cycling improvement of E. coli.     

Production of specific-molecular-weight hyaluronan by metabolically engineered Bacillus subtilis 168

Low-molecular-weight hyaluronan (LMW-HA) has attracted much attention because of its many potential applications. Here, we efficiently produced specific LMW-HAs from sucrose in Bacillus subtilis. By coexpressing the identified committed genes (tuaD, gtaB, glmU, glmM, and glmS) and downregulating the glycolytic pathway, HA production was significantly increased from 1.01 g L⁻¹ to 3.16 g L⁻¹, with a molecular weight range of 1.40×10⁶–1.83×10⁶ Da. When leech hyaluronidase was actively expressed after N-terminal engineering (1.62×10⁶ U mL⁻¹), the production of HA was substantially increased from 5.96 g L⁻¹ to 19.38 g L⁻¹. The level of hyaluronidase was rationally regulated with a ribosome-binding site engineering strategy, allowing the production of LMW-HAs with a molecular weight range of 2.20×10³–1.42×10⁶ Da. Our results confirm that this strategy for the controllable expression of hyaluronidase, together with the optimization of the HA synthetic pathway, effectively produces specific LMW-HAs, and could also be used to produce other LMW polysaccharides.     

Bio-based succinate from sucrose: High-resolution 13C metabolic flux analysis and metabolic engineering of the rumen bacterium Basfia succiniciproducens

Succinic acid is a platform chemical of recognized industrial value and accordingly faces a continuous challenge to enable manufacturing from most attractive raw materials. It is mainly produced from glucose, using microbial fermentation. Here, we explore and optimize succinate production from sucrose, a globally applied substrate in biotechnology, using the rumen bacterium Basfia succiniciproducens DD1. As basis of the strain optimization, the yet unknown sucrose metabolism of the microbe was studied, using ¹³C metabolic flux analyses. When grown in batch culture on sucrose, the bacterium exhibited a high succinate yield of 1 mol mol⁻¹ and a by-product spectrum, which did not match the expected PTS-mediated sucrose catabolism. This led to the discovery of a fructokinase, involved in sucrose catabolism. The flux approach unraveled that the fructokinase and the fructose PTS both contribute to phosphorylation of the fructose part of sucrose. The contribution of the fructokinase reduces the undesired loss of the succinate precursor PEP into pyruvate and into pyruvate-derived by-products and enables increased succinate production, exclusively via the reductive TCA cycle branch. These findings were used to design superior producers. Mutants, which (i) overexpress the beneficial fructokinase, (II) lack the competing fructose PTS, and (iii) combine both traits, produce significantly more succinate. In a fed-batch process, B. succiniciproducens ΔfruA achieved a titer of 71 g L⁻¹ succinate and a yield of 2.5 mol mol⁻¹ from sucrose.     

Rapid ethanol production at elevated temperatures by engineered thermotolerant Kluyveromyces marxianus via the NADP(H)-preferring xylose reductase-xylitol dehydrogenase pathway

Conversion of xylose to ethanol by yeasts is a challenge because of the redox imbalances under oxygen-limited conditions. The thermotolerant yeast Kluyveromyces marxianus grows well with xylose as a carbon source at elevated temperatures, but its xylose fermentation ability is weak. In this study, a combination of the NADPH-preferring xylose reductase (XR) from Neurospora crassa and the NADP⁺-preferring xylitol dehydrogenase (XDH) mutant from Scheffersomyces stipitis (Pichia stipitis) was constructed. The xylose fermentation ability and redox balance of the recombinant strains were improved significantly by over-expression of several downstream genes. The intracellular concentrations of coenzymes and the reduced coenzyme/oxidized coenzyme ratio increased significantly in these metabolic strains. The byproducts, such as glycerol and acetic acid, were significantly reduced by the disruption of glycerol-3-phosphate dehydrogenase (GPD1). The resulting engineered K. marxianus YZJ088 strain produced 44.95 g/L ethanol from 118.39 g/L xylose with a productivity of 2.49 g/L/h at 42 °C. Additionally, YZJ088 realized glucose and xylose co-fermentation and produced 51.43 g/L ethanol from a mixture of 103.97 g/L xylose and 40.96 g/L glucose with a productivity of 2.14 g/L/h at 42 °C. These promising results validate the YZJ088 strain as an excellent producer of ethanol from xylose through the synthetic xylose assimilation pathway.     

Production of glucaric acid from myo-inositol in engineered Pichia pastoris

A potential myo-inositol oxygenase (ppMIOX) was identified as a functional enzyme and a glucaric acid synthetic pathway was firstly constructed in Pichia pastoris. Coexpression of the native ppMIOX and the urinate dehydrogenase (Udh) from Pseudomonas putida KT2440 led to obvious accumulation of glucaric acid (90.46 ± 0.04 mg/L) from myo-inositol whereas no glucaric acid was detected from glucose. In comparison, coexpression of the heterologous mouse MIOX (mMIOX) and Udh resulted in higher titers of glucaric acid from glucose and myo-inositol, 107.19 ± 11.91 mg/L and 785.4 ± 1.41 mg/L, respectively. By applying a fusion expression strategy with flexible peptides, the mMIOX specific activity and the glucaric acid concentration were significantly increased. Using glucose and myo-inositol as carbon substrates, the production of glucaric acid was substantially enhanced to 6.61 ± 0.30 g/L in fed-batch cultures. To the best of our knowledge, this is the highest reported value to date.     

Introduction of a bacterial acetyl-CoA synthesis pathway improves lactic acid production in Saccharomyces cerevisiae

Acid-tolerant Saccharomyces cerevisiae was engineered to produce lactic acid by expressing heterologous lactate dehydrogenase (LDH) genes, while attenuating several key pathway genes, including glycerol-3-phosphate dehydrogenase1 (GPD1) and cytochrome-c oxidoreductase2 (CYB2). In order to increase the yield of lactic acid further, the ethanol production pathway was attenuated by disrupting the pyruvate decarboxylase1 (PDC1) and alcohol dehydrogenase1 (ADH1) genes. Despite an increase in lactic acid yield, severe reduction of the growth rate and glucose consumption rate owing to the absence of ADH1 caused a considerable decrease in the overall productivity. In Δadh1 cells, the levels of acetyl-CoA, a key precursor for biologically applicable components, could be insufficient for normal cell growth. To increase the cellular supply of acetyl-CoA, we introduced bacterial acetylating acetaldehyde dehydrogenase (A-ALD) enzyme (EC 1.2.1.10) genes into the lactic acid-producing S. cerevisiae. Escherichia coli-derived A-ALD genes, mhpF and eutE, were expressed and effectively complemented the attenuated acetaldehyde dehydrogenase (ALD)/acetyl-CoA synthetase (ACS) pathway in the yeast. The engineered strain, possessing a heterologous acetyl-CoA synthetic pathway, showed an increased glucose consumption rate and higher productivity of lactic acid fermentation. The production of lactic acid was reached at 142 g/L with production yield of 0.89 g/g and productivity of 3.55 g L⁻¹ h⁻¹ under fed-batch fermentation in bioreactor. This study demonstrates a novel approach that improves productivity of lactic acid by metabolic engineering of the acetyl-CoA biosynthetic pathway in yeast.     

Metabolic engineering of Corynebacterium glutamicum for the de novo production of ethylene glycol from glucose

Development of sustainable biological process for the production of bulk chemicals from renewable feedstock is an important goal of white biotechnology. Ethylene glycol (EG) is a large-volume commodity chemical with an annual production of over 20 million tons, and it is currently produced exclusively by petrochemical route. Herein, we report a novel biosynthetic route to produce EG from glucose by the extension of serine synthesis pathway of Corynebacterium glutamicum. The EG synthesis is achieved by the reduction of glycoaldehyde derived from serine. The transformation of serine to glycoaldehyde is catalyzed either by the sequential enzymatic deamination and decarboxylation or by the enzymatic decarboxylation and oxidation. We screened the corresponding enzymes and optimized the production strain by combinatorial optimization and metabolic engineering. The best engineered C. glutamicum strain is able to accumulate 3.5 g/L of EG with the yield of 0.25 mol/mol glucose in batch cultivation. This study lays the basis for developing an efficient biological process for EG production.     

Cu-mediated biomass productivity enhancement and lutein enrichment of the novel microalga Coccomyxa onubensis

The influence of Cu (II) on productivity and accumulation of value carotenoids of a microalga that naturally grows at low pH, Coccomyxa onubensis, was investigated. The presence of Cu (II), added in range between 0.06 and 0.4 mM, increases both algal viability and synthesis of carotenoids, mostly lutein and β-carotene. A copper concentration of 0.2 mM was found to be as the most appropriate one to enhance productivity and lutein accumulation and was further used in semicontinuous cultures. Unlike acidophile microalgae, C. onubensis showed unusual high growth rates (0.50 d^?1) when cultured semicontinuously at 0.2 mM Cu (II) and getting an average productivity of 0.42 g l^?1 d^?1. Lutein content in 0.2 mM Cu (II) cultures was roughly 50% higher than that obtained for control cultures. C. onubensis seems to have great potential as lutein producer when compared to known lutein accumulating microalgae. C. onubensis is able to live in highly selective environment, which confers the microalga a competitive advantage over other organisms that cannot survive at such low pH and high concentrations of heavy metals. This might make of C. onubensis a unique alga for large producer in open systems.     

Metabolic engineering of Clostridium tyrobutyricum for enhanced butyric acid production from glucose and xylose

Clostridium tyrobutyricum is a promising microorganism for butyric acid production. However, its ability to utilize xylose, the second most abundant sugar found in lignocellulosic biomass, is severely impaired by glucose-mediated carbon catabolite repression (CCR). In this study, CCR in C. tyrobutyricum was eliminated by overexpressing three heterologous xylose catabolism genes (xylT, xylA and xlyB) cloned from C. acetobutylicum. Compared to the parental strain, the engineered strain Ct-pTBA produced more butyric acid (37.8 g/L vs. 19.4 g/L) from glucose and xylose simultaneously, at a higher xylose utilization rate (1.28 g/L·h vs. 0.16 g/L·h) and efficiency (94.3% vs. 13.8%), resulting in a higher butyrate productivity (0.53 g/L·h vs. 0.26 g/L·h) and yield (0.32 g/g vs. 0.28 g/g). When the initial total sugar concentration was ~120 g/L, both glucose and xylose utilization rates increased with increasing their respective concentration or ratio in the co-substrates but the total sugar utilization rate remained almost unchanged in the fermentation at pH 6.0. Decreasing the pH to 5.0 significantly decreased sugar utilization rates and butyrate productivity, but the effect was more pronounced for xylose than glucose. The addition of benzyl viologen (BV) as an artificial electron carrier facilitated the re-assimilation of acetate and increased butyrate production to a final titer of 46.4 g/L, yield of 0.43 g/g sugar consumed, productivity of 0.87 g/L·h, and acid purity of 98.3% in free-cell batch fermentation, which were the highest ever reported for butyric acid fermentation. The engineered strain with BV addition thus can provide an economical process for butyric acid production from lignocellulosic biomass.     

Evaluation of distant carbon sources in biosurfactant production by a gamma ray-induced Pseudomonas putida mutant

Pseudomonas putida 33 wild strain, subjected to gamma ray mutagenesis and designated as P. putida 300-B mutant was used as microbial rhamnolipid-producer by using distant carbon sources (viz. hydrocarbons, waste frying oils ‘WFOs’, vegetable oil refinery wastes and molasses) in the minimal media under shake flask conditions. The behavior of glucose as co-substrate and growth initiator was examined. The 300-B mutant strain showed its ability to grow on all the substrates tested and produced rhamnolipid surfactants to different extents however; soybean and corn WFOs were observed to be preferred carbon sources followed by kerosene and paraffin oils, respectively. The best cell biomass (3.5 g l⁻¹) and rhamnolipids yield (4.1 g l⁻¹) were obtained with soybean WFO as carbon source and glucose as growth initiator under fed-batch cultivation showing an optimum specific growth rate (μ) of 0.272 h⁻¹, specific product yield (q_p) of 0.318 g g⁻¹ h and volumetric productivity (P_V) of 0.024 g l⁻¹ h. The critical micelle concentration of its culture supernatant was observed to be 91 mg rhamnolipids l⁻¹ and surface tension as 31.2 mN m⁻¹.