Engineering cofactor and transport mechanisms in Saccharomyces cerevisiae for enhanced acetyl-CoA and polyketide biosynthesis

Synthesis of polyketides at high titer and yield is important for producing pharmaceuticals and biorenewable chemical precursors. In this work, we engineered cofactor and transport pathways in Saccharomyces cerevisiae to increase acetyl-CoA, an important polyketide building block. The highly regulated yeast pyruvate dehydrogenase bypass pathway was supplemented by overexpressing a modified Escherichia coli pyruvate dehydrogenase complex (PDHm) that accepts NADP⁺ for acetyl-CoA production. After 24 h of cultivation, a 3.7-fold increase in NADPH/NADP⁺ ratio was observed relative to the base strain, and a 2.2-fold increase relative to introduction of the native E. coli PDH. Both E. coli pathways increased acetyl-CoA levels approximately 2-fold relative to the yeast base strain. Combining PDHm with a ZWF1 deletion to block the major yeast NADPH biosynthesis pathway resulted in a 12-fold NADPH boost and a 2.2-fold increase in acetyl-CoA. At 48 h, only this coupled approach showed increased acetyl-CoA levels, 3.0-fold higher than that of the base strain. The impact on polyketide synthesis was evaluated in a S. cerevisiae strain expressing the Gerbera hybrida 2-pyrone synthase (2-PS) for the production of the polyketide triacetic acid lactone (TAL). Titers of TAL relative to the base strain improved only 30% with the native E. coli PDH, but 3.0-fold with PDHm and 4.4-fold with PDHm in the Δzwf1 strain. Carbon was further routed toward TAL production by reducing mitochondrial transport of pyruvate and acetyl-CoA; deletions in genes POR2, MPC2, PDA1, or YAT2 each increased titer 2–3-fold over the base strain (up to 0.8 g/L), and in combination to 1.4 g/L. Combining the two approaches (NADPH-generating acetyl-CoA pathway plus reduced metabolite flux into the mitochondria) resulted in a final TAL titer of 1.6 g/L, a 6.4-fold increase over the non-engineered yeast strain, and 35% of theoretical yield (0.16 g/g glucose), the highest reported to date. These biological driving forces present new avenues for improving high-yield production of acetyl-CoA derived compounds.     

谷氨酸棒杆菌代谢工程高效生产L-缬氨酸北大核心CSCD

L-缬氨酸作为一种支链氨基酸,广泛应用于医药和饲料等领域。本研究借助多种代谢工程策略相结合的方法,构建了生产L-缬氨酸的微生物细胞工厂,实现了L-缬氨酸的高效生产。首先,通过增强糖酵解途径、减弱副产物代谢途径相结合的方式,强化了L-缬氨酸合成前体丙酮酸的供给;其次,针对L-缬氨酸合成路径关键酶—乙酰羟酸合酶进行定点突变,提高了菌株的抗反馈抑制能力,并利用启动子工程策略,优化了路径关键酶的基因表达水平;最后,利用辅因子工程策略,改变了乙酰羟酸还原异构酶和支链氨基酸转氨酶的辅因子偏好性,由偏好NADPH转变为偏好NADH,从而提高了L-缬氨酸的合成能力。在5L发酵罐中,最优谷氨酸棒杆菌工程菌株Corynebacterium glutamicum K020的L-缬氨酸产量、得率和生产强度分别达到了110g/L、0.51g/g和2.29 g/(L·h)。     

Systems metabolic engineering of Corynebacterium glutamicum for the efficient production of β-alanine

β-Alanine is an important β-amino acid with a growing demand in a wide range of applications in chemical and food industries. However, current industrial production of β-alanine relies on chemical synthesis, which usually involves harmful raw materials and harsh production conditions. Thus, there has been increasing demand for more sustainable, yet efficient production process of β-alanine. In this study, we constructed Corynebacterium glutamicum strains for the highly efficient production of β-alanine through systems metabolic engineering. First, aspartate 1-decarboxylases (ADCs) from seven different bacteria were screened, and the Bacillus subtilis ADC showing the most efficient β-alanine biosynthesis was used to construct a β-alanine-producing base strain. Next, genome-scale metabolic simulations were conducted to optimize multiple metabolic pathways in the base strain, including phosphotransferase system (PTS)-independent glucose uptake system and the biosynthesis of key precursors, including oxaloacetate and L-aspartate. TCA cycle was further engineered for the streamlined supply of key precursors. Finally, a putative β-alanine exporter was newly identified, and its overexpression further improved the β-alanine production. Fed-batch fermentation of the final engineered strain BAL10 (pBA2_tr18) produced 166.6 g/L of β-alanine with the yield and productivity of 0.28 g/g glucose and 1.74 g/L/h, respectively. To our knowledge, this production performance corresponds to the highest titer, yield and productivity reported to date for the microbial fermentation.     

Metabolic engineering of Escherichia coli for efficient free fatty acid production from glycerol

Crude glycerol, generated as waste by-product in biodiesel production process, has been considered as an important carbon source for converting to value-added bioproducts recently. Free fatty acids (FFAs) can be used as precursors for the production of biofuels or biochemicals. Microbial biosynthesis of FFAs can be achieved by introducing an acyl–acyl carrier protein thioesterase into Escherichia coli. In this study, the effect of metabolic manipulation of FFAs synthesis cycle, host genetic background and cofactor engineering on FFAs production using glycerol as feed stocks was investigated. The highest concentration of FFAs produced by the engineered stain reached 4.82 g/L with the yield of 29.55% (g FFAs/g glycerol), about 83% of the maximum theoretical pathway value by the type II fatty acid synthesis pathway. In addition, crude glycerol from biodiesel plant was also used as feedstock in this study. The FFA production was 3.53 g/L with a yield of 24.13%. The yield dropped slightly when crude glycerol was used as a carbon source instead of pure glycerol, while it still can reach about 68% of the maximum theoretical pathway yield.     

Engineering of carboligase activity reaction in Candida glabrata for acetoin production

Utilization of Candida glabrata overproducing pyruvate is a promising strategy for high-level acetoin production. Based on the known regulatory and metabolic information, acetaldehyde and thiamine were fed to identify the key nodes of carboligase activity reaction (CAR) pathway and provide a direction for engineering C. glabrata. Accordingly, alcohol dehydrogenase, acetaldehyde dehydrogenase, pyruvate decarboxylase, and butanediol dehydrogenase were selected to be manipulated for strengthening the CAR pathway. Following the rational metabolic engineering, the engineered strain exhibited increased acetoin biosynthesis (2.24 g/L). In addition, through in silico simulation and redox balance analysis, NADH was identified as the key factor restricting higher acetoin production. Correspondingly, after introduction of NADH oxidase, the final acetoin production was further increased to 7.33 g/L. By combining the rational metabolic engineering and cofactor engineering, the acetoin-producing C. glabrata was improved stepwise, opening a novel pathway for rational development of microorganisms for bioproduction.     

Direct biosynthesis of adipic acid from lignin-derived aromatics using engineered Pseudomonas putida KT2440

Lignin is one largely untapped natural resource that can be exploited as a raw material for the bioproduction of value-added chemicals. Meanwhile, the current petroleum-based process for the production of adipic acid faces sustainability challenges. Here we report the successful engineering of Pseudomonas putida KT2440 strain for the direct biosynthesis of adipic acid from lignin-derived aromatics. The devised bio-adipic acid route features an artificial biosynthetic pathway that is connected to the endogenous aromatics degradation pathway of the host at the branching point, 3-ketoadipoyl-CoA, by taking advantage of the unique carbon skeleton of this key intermediate. Studies of the metabolism of 3-ketoadipoyl-CoA led to the discovery of crosstalk between two aromatics degradation pathways in KT2440. This knowledge facilitated the formulation and implementation of metabolic engineering strategies to optimize the carbon flux into the biosynthesis of adipic acid. By optimizing pathway expression and cultivation conditions, an engineered strain AA-1 produced adipic acid at 0.76 g/L and 18.4% molar yield under shake-flask conditions and 2.5 g/L and 17.4% molar yield under fermenter-controlled conditions from common aromatics that can be derived from lignin. This represents the first example of the direct adipic acid production from model compounds of lignin depolymerization.     

Stepwise increase of resveratrol biosynthesis in yeast Saccharomyces cerevisiae by metabolic engineering

Resveratrol is a unique, natural polyphenolic compound with diverse health benefits. In the present study, we attempted to improve resveratrol biosynthesis in yeast by different methods of metabolic engineering. We first mutated and then re-synthesized tyrosine ammonia lyase (TAL) by replacing the bacteria codons with yeast-preferred codons, which increased translation and improved p-coumaric acid and resveratrol biosynthesis drastically. We then demonstrated that low-affinity, high-capacity bacterial araE transporter could enhance resveratrol accumulation, without transporting resveratrol directly. Yeast cells carrying the araE gene produced up to 2.44-fold higher resveratrol than control cells. For commercial applications, resveratrol biosynthesis was detected in sucrose medium and fresh grape juice using our engineered yeast cells. In collaboration with the Chaumette Winery of Missouri, we were able to produce resveratrol-containing white wines, with levels comparable to the resveratrol levels found in most red wines.     

High-yield production of L-valine in engineered Escherichia coli by a novel two-stage fermentation

L-valine is an essential amino acid and an important amino acid in the food and feed industry. The relatively low titer and low fermentation yield currently limit the large-scale application of L-valine. Here, we constructed a chromosomally engineered Escherichia coli to efficiently produce L-valine. First, the synthetic pathway of L-valine was enhanced by heterologous introduction of a feedback-resistant acetolactate acid synthase from Bacillus subtilis and overexpression of other two enzymes in the L-valine synthetic pathway. For efficient efflux of L-valine, an exporter from Corynebacterium glutamicum was subsequently introduced. Next, the precursor pyruvate pool was increased by knockout of GTP pyrophosphokinase and introduction of a ppGpp 3′-pyrophosphohydrolase mutant to facilitate the glucose uptake process. Finally, in order to improve the redox cofactor balance, acetohydroxy acid isomeroreductase was replaced by a NADH-preferring mutant, and branched-chain amino acid aminotransferase was replaced by leucine dehydrogenase from Bacillus subtilis. Redox cofactor balance enabled the strain to synthesize L-valine under oxygen-limiting condition, significantly increasing the yield in the presence of glucose. Two-stage fed-batch fermentation of the final strain in a 5 L bioreactor produced 84 g/L L-valine with a yield and productivity of 0.41 g/g glucose and 2.33 g/L/h, respectively. To the best of our knowledge, this is the highest L-valine titer and yield ever reported in E. coli. The systems metabolic engineering strategy described here will be useful for future engineering of E. coli strains for the industrial production of L-valine and related products.     

Engineering of biotin-prototrophy in Pichia pastoris for robust production processes

Biotin plays an essential role as cofactor for biotin-dependent carboxylases involved in essential metabolic pathways. The cultivation of Pichia pastoris, a methylotrophic yeast that is successfully used as host for the production of recombinant proteins, requires addition of high dosage of biotin. As biotin is the only non-salt media component used during P. pastoris fermentation (apart from the carbon source), nonconformities during protein production processes are usually attributed to poor quality of the added biotin.In order to avoid dismissed production runs due to biotin quality issues, we engineered the biotin-requiring yeast P. pastoris to become a biotin-prototrophic yeast. Integration of four genes involved in the biotin biosynthesis from brewing yeast into the P. pastoris genome rendered P. pastoris biotin-prototrophic. The engineered strain has successfully been used as production host for both intracellular and secreted heterologous proteins in fed-batch processes, employing mineral media without vitamins. Another field of application for these truly prototrophic hosts is the production of biochemicals and small metabolites, where defined mineral media leads to easier purification procedures.     

Dynamic control over feedback regulatory mechanisms improves NADPH flux and xylitol biosynthesis in engineered E. coli

We report improved NADPH flux and xylitol biosynthesis in engineered E. coli. Xylitol is produced from xylose via an NADPH dependent reductase. We utilize 2-stage dynamic metabolic control to compare two approaches to optimize xylitol biosynthesis, a stoichiometric approach, wherein competitive fluxes are decreased, and a regulatory approach wherein the levels of key regulatory metabolites are reduced. The stoichiometric and regulatory approaches lead to a 20-fold and 90-fold improvement in xylitol production, respectively. Strains with reduced levels of enoyl-ACP reductase and glucose-6-phosphate dehydrogenase, led to altered metabolite pools resulting in the activation of the membrane bound transhydrogenase and an NADPH generation pathway, consisting of pyruvate ferredoxin oxidoreductase coupled with NADPH dependent ferredoxin reductase, leading to increased NADPH fluxes, despite a reduction in NADPH pools. These strains produced titers of 200 g/L of xylitol from xylose at 86% of theoretical yield in instrumented bioreactors. We expect dynamic control over the regulation of the membrane bound transhydrogenase as well as NADPH production through pyruvate ferredoxin oxidoreductase to broadly enable improved NADPH dependent bioconversions or production via NADPH dependent metabolic pathways.     

Engineering precursor supply for the high-level production of ergothioneine in Saccharomyces cerevisiae

Ergothioneine (ERG) is an unusual sulfur-containing amino acid. It is a potent antioxidant, which shows great potential for ameliorating neurodegenerative and cardiovascular diseases. L-ergothioneine is rare in nature, with mushrooms being the primary dietary source. The chemical synthesis process is complex and expensive. Alternatively, ERG can be produced by fermentation of recombinant microorganisms engineered for ERG overproduction. Here, we describe the engineering of S. cerevisiae for high-level ergothioneine production on minimal medium with glucose as the only carbon source. To this end, metabolic engineering targets in different layers of the amino acid metabolism were selected based on literature and tested. Out of 28 targets, nine were found to improve ERG production significantly by 10%–51%. These targets were then sequentially implemented to generate an ergothioneine-overproducing yeast strain capable of producing 106.2 ± 2.6 mg/L ERG in small-scale cultivations. Transporter engineering identified that the native Aqr1 transporter was capable of increasing the ERG production in a yeast strain with two copies of the ERG biosynthesis pathway, but not in the strain that was further engineered for improved precursor supply. Medium optimization indicated that additional supplementation of pantothenate improved the strain's productivity further and that no supplementation of amino acid precursors was necessary. Finally, the engineered strain produced 2.39 ± 0.08 g/L ERG in 160 h (productivity of 14.95 ± 0.49 mg/L/h) in a controlled fed-batch fermentation without supplementation of amino acids. This study paves the way for the low-cost fermentation-based production of ergothioneine.     

Modular pathway engineering of key carbon‐precursor supply‐pathways for improved N‐acetylneuraminic acid production in Bacillus subtilis

N‐acetylneuraminic acid (NeuAc) is widely used as a nutraceutical for facilitating infant brain development, maintaining brain health, and enhancing immunity. Currently, NeuAc is mainly produced by extraction from egg yolk and milk, or via chemical synthesis. However, its low concentration in natural resources and its non‐ecofriendly chemical synthesis result in insufficient NeuAc production and environmental pollution, respectively. In this study, improved NeuAc production was attained via modular pathway engineering of the supply pathways of two key precursors—N‐acetylglucosamine (GlcNAc) and phosphoenolpyruvate (PEP)—and by balancing NeuAc biosynthesis and cell growth in engineered Bacillus subtilis. Specifically, we used a previously constructed GlcNAc‐producing B. subtilis as the initial host for NeuAc biosynthesis. First, we constructed a de novo NeuAc biosynthetic pathway utilizing glucose by coexpressing glucosamine‐6‐phosphate acetyl‐transferase (GNA1), N‐acetylglucosamine 2‐epimerase (AGE), and N‐acetylneuraminic acid synthase (NeuB), resulting in 0.33 g/l NeuAc production. Next, to balance the supply of the two key precursors for NeuAc biosynthesis, modular pathway engineering was performed. The optimal strategy for balancing the GlcNAc module and PEP supply module involved the use of an engineered, unique glucose and malate coutilization pathway in B. subtilis, supplied with both glucose (for the GlcNAc moiety) and malate (for the PEP moiety) at high strength. This led to 1.65 g/L NeuAc production, representing a 5.0‐fold improvement over the existing methods. Furthermore, to enhance the NeuAc yield on cell, glucose and malate coutilization pathways were engineered to balance NeuAc biosynthesis and cell growth via the blocking of glycolysis, the introduction of the Entner–Doudoroff pathway, and the overexpression of the malic enzyme YtsJ. NeuAc titer reached 2.18 g/L, with 0.38 g/g dry cell weight NeuAc yield on cell, which represented a 1.32‐fold and 2.64‐fold improvement over the existing methods, respectively. The strategy of modular pathway engineering of key carbon precursor supply pathways via engineering of the unique glucose‐malate coutilization pathway in B. subtilis should be generically applicable for engineering of B. subtilis for the production of other important biomolecules. Our study also provides a good starting point for further metabolic engineering to achieve industrial production of NeuAc by a Generally Regarded As Safe bacterial strain.     

Utilization of Saccharomyces cerevisiae recombinant strain incapable of both ethanol and glycerol biosynthesis for anaerobic bioproduction

The yeast Saccharomyces cerevisiae produces ethanol and glycerol as major unwanted byproducts, unless ethanol and glycerol are the target compounds. Minimizing the levels of these byproducts is important for bioproduction processes using yeast cells. In this study, we constructed a yeast strain in which both ethanol and glycerol production pathways were disrupted and examined its culture characteristics. In wild-type yeast strain, metabolic pathways that produce ethanol and glycerol play an important role in reoxidizing nicotinamide adenine dinucleotide (NADH) generated during glycolysis, particularly under anaerobic conditions. Strains in which both pathways were disrupted therefore failed to grow and consume glucose under anaerobic conditions. Introduction of desired metabolic reaction(s) coupled with NADH oxidation enabled the engineered strain to consume substrate and produce target compound(s). Here we introduced NADH-oxidization-coupled L-lactate production mechanisms into a yeast strain incapable of ethanol and glycerol biosynthesis, based on in silico simulation using a genome-scale metabolic model of S. cerevisiae. From the results of in silico simulation based on flux balance analysis, a feasible anaerobic non-growing metabolic state, in which L-lactate yield approached the theoretical maximum, was identified and this phenomenon was verified experimentally. The yeast strain incapable of both ethanol and glycerol biosynthesis is a potentially valuable host for bioproduction coupled with NADH oxidation under anaerobic conditions.     

定向进化改造酪氨酸解氨酶提高大肠杆菌合成对香豆酸产量

对香豆酸是一种具有多种药理活性的天然酚类化合物,也是多种天然药用产物生物合成的前体物质,广泛应用于食品、化妆品、医药等领域。通过微生物合成对香豆酸相对于化学合成和植物提取工艺具有节能减排等优势。但是,目前微生物合成对香豆酸产量较低,难以满足大规模工业发酵生产的要求。为了进一步提高对香豆酸产量,对粘红酵母酪氨酸解氨酶 (Tyrosine ammonia-lyase,TAL) 进行定向进化改造,利用高通量筛选方法从随机突变体文库中筛选TAL催化活性提高的突变体。通过初筛和复筛两轮筛选,从大约10 000个突变体中获得1个TAL催化活性提高1倍的突变体。该突变体包含3个氨基酸突变位点,分别为S9Y、A11N、E518A。进一步通过单点氨基酸饱和突变验证,当S9位点突变为Y、I、N和A11位点突变为N、T、Y时,TAL的催化活性提高1倍以上。通过对S9和A11位点3种类型突变进行组合突变验证,S9Y/A11N和S9N/A11Y突变体的TAL催化活力显著高于其他组合。将S9N/A11Y突变体质粒转入酪氨酸高产菌株CP032。通过摇瓶发酵,该菌株在48 h时的对香豆酸产量达到394.2 mg/L,比对照菌提高2.2倍。本研究工作对促进微生物合成对香豆酸的代谢工程研究具有一定的参考价值。     

Synthesis of polyketides from low cost substrates by the thermotolerant yeast Kluyveromyces marxianus

Kluyveromyces marxianus is a promising nonconventional yeast for biobased chemical production due to its rapid growth rate, high TCA cycle flux, and tolerance to low pH and high temperature. Unlike Saccharomyces cerevisiae, K. marxianus grows on low-cost substrates to cell densities that equal or surpass densities in glucose, which can be beneficial for utilization of lignocellulosic biomass (xylose), biofuel production waste (glycerol), and whey (lactose). We have evaluated K. marxianus for the synthesis of polyketides, using triacetic acid lactone (TAL) as the product. The 2-pyrone synthase (2-PS) was expressed on a CEN/ARS plasmid in three different strains, and the effects of temperature, carbon source, and cultivation strategy on TAL levels were determined. The highest titer was obtained in defined 1% xylose medium at 37°C, with substantial titers at 41 and 43°C. The introduction of a high-stability 2-PS mutant and a promoter substitution increased titer four-fold. 2-PS expression from a multi-copy pKD1-based plasmid improved TAL titers a further five-fold. Combining the best plasmid, promoter, and strain resulted in a TAL titer of 1.24 g/L and a yield of 0.0295 mol TAL/mol carbon for this otherwise unengineered strain in 3 ml tube culture. This is an excellent titer and yield (on xylose) before metabolic engineering or fed-batch culture relative to other hosts (on glucose), and demonstrates the promise of this rapidly growing and thermotolerant yeast species for polyketide production.