代谢工程改造大肠杆菌合成丁二酸及发酵罐放大工艺

【背景】Escherichia coli AFP111发酵生产丁二酸时大量副产乙酸,丁二酸得率低。【目的】代谢工程改造EscherichiacoliAFP111,提高丁二酸得率,降低副产物乙酸的生成,建立100 L规模的丁二酸发酵工艺。【方法】一步同源重组敲除乙酸合成途径关键酶基因,改造丁二酸合成途径关键酶启动子实现过表达;单因素优化5L发酵罐培养条件。【结果】敲除乙酸产生途径编码乙酸激酶和磷酸转乙酰酶的基因ackA-pta、苏氨酸脱羧酶和2-酮丁酸甲酸裂解酶的基因tdcDE获得SX02菌株,摇瓶发酵条件下其乙酸产量下降了53.42%,丁二酸得率提高9.85%。在SX02菌株基础上,经启动子改造过表达编码葡萄糖激酶的基因glk后获得菌株SX03,其Glk酶活性提高3.66倍,乙酸产量下降了31.62%,丁二酸得率提高8.28%。SX03菌株发酵生产丁二酸在5 L发酵罐进行放大,其乙酸产量为3.97 g/L,丁二酸得率为1.62 mol/mol葡萄糖,相比出发菌株的乙酸产量下降了75.76%,丁二酸得率提高19.12%。在5L发酵罐上对比研究了中和剂Na2CO3和NaOH混合液替换碱式MgCO3的发酵效果,并优化了发酵pH、搅拌转速和葡萄糖浓度,获得如下最适发酵条件:pH6.8,搅拌转速250r/min,葡萄糖100g/L,发酵结束时乙酸产量为2.24 g/L,丁二酸得率为1.66 mol/mol葡萄糖。中和剂替换优化后乙酸产量下降了20.65%,丁二酸得率提高2.47%。菌株SX03发酵工艺进一步在100 L发酵罐上实现放大,其乙酸产量为1.91 g/L,丁二酸得率为1.30 mol/mol葡萄糖。【结论】通过代谢工程改造的大肠杆菌,其副产物乙酸含量显著下降,丁二酸得率提高,并在5 L和100 L发酵罐上实现了工艺放大,展现出较大的工业化利用潜力。     

Prospects for a bio-based succinate industry

Bio-based succinate is receiving increasing attention as a potential intermediary feedstock for replacing a large petrochemical-based bulk chemical market. The prospective economical and environmental benefits of a bio-based succinate industry have motivated research and development of succinate-producing organisms. Bio-based succinate is still faced with the challenge of becoming cost competitive against petrochemical-based alternatives. High succinate concentrations must be produced at high rates, with little or no by-products to most efficiently use substrates and to simplify purification procedures. Herein are described the current prospects for a bio-based succinate industry, with emphasis on specific bacteria that show the greatest promise for industrial succinate production. The succinate-producing characteristics and the metabolic pathway used by each bacterial species are described, and the advantages and disadvantages of each bacterial system are discussed.     

Metabolic engineering of cyanobacteria for the photosynthetic production of succinate

Succinate is an important commodity chemical currently used in the food, pharmaceutical, and polymer industries. It can also be chemically converted into other major industrial chemicals such as 1,4-butanediol, butadiene, and tetrahydrofuran. Here we metabolically engineered a model cyanobacterium Synechococcus elongatus PCC 7942 to photosynthetically produce succinate. We expressed the genes encoding for α-ketoglutarate decarboxylase and succinate semialdehyde dehydrogenase in S. elongatus PCC 7942, resulting in a strain capable of producing 120 mg/L of succinate. However, this recombinant strain exhibited severe growth retardation upon induction of the genes encoding for the succinate producing pathway, potentially due to the depletion of α-ketoglutarate. To replenish α-ketoglutarate, we expressed the genes encoding for phosphoenolpyruvate carboxylase and citrate synthase from Corynebacterium glutamicum into the succinate producing strain. The resulting strain successfully restored the growth phenotype and produced succinate with a titer of 430 mg/L in 8 days. These results demonstrated the possibility of photoautotrophic succinate production.     

Batch culture characterization and metabolic flux analysis of succinate-producing Escherichia coli strains

This study presents an in-depth analysis of the anaerobic metabolic fluxes of various mutant strains of Escherichia coli overexpressing the Lactococcus lactis pyruvate carboxylase (PYC) for the production of succinate. Previously, a metabolic network design that includes an active glyoxylate pathway implemented in vivo increased succinate yield from glucose in an E. coli mutant to 1.6 mol/mol under fully anaerobic conditions. The design consists of a dual succinate synthesis route, which diverts required quantities of NADH through the traditional fermentative pathway and maximizes the carbon converted to succinate by balancing the carbon flux through the fermentative pathway and the glyoxylate pathway (which has a lower NADH requirement). Mutant strains previously constructed during the development of high-yield succinate-producing strains were selected for further characterization to understand their metabolic response as a result of several genetic manipulations and to determine the significance of the fermentative and the glyoxylate pathways in the production of succinate. Measured fluxes obtained under batch cultivation conditions were used to estimate intracellular fluxes and identify critical branch point flux split ratios. The comparison of changes in branch point flux split ratios to the glyoxylate pathway and the fermentative pathway at the oxaloacetate (OAA) node as a result of different mutations revealed the sensitivity of succinate yield to these manipulations. The most favorable split ratio to obtain the highest succinate yield was the fractional partition of OAA to glyoxylate of 0.32 and 0.68 to the fermentative pathway obtained in strains SBS550MG (pHL413) and SBS990MG (pHL413). The succinate yields achieved in these two strains were 1.6 and 1.7 mol/mol, respectively. In addition, an active glyoxylate pathway in an ldhA, adhE, ack-pta mutant strain is shown to be responsible for the high succinate yields achieved anaerobically. Furthermore, in vitro activity measurements of seven crucial enzymes involved in the pathways studied and intracellular measurements of key intermediate metabolite pools provided additional insights on the physiological perturbations caused by these mutations. The characterization of these recombinant mutant strains in terms of flux distribution pattern, in vitro enzyme activity and intracellular metabolite pools provides useful information for the rational modification of metabolic fluxes to improve succinate production.     

系统代谢工程改造树干毕赤酵母生产琥珀酸

为提高树干毕赤酵母发酵生产琥珀酸的产量,借助基因组规模代谢网络模型iTL885获得琥珀酸合成的最佳代谢途径为扩增icl1基因和敲除sdh1基因。在此基础上,借助代谢工程策略构建过量表达异柠檬酸裂解酶基因icl1的重组菌株FPLicl、缺失琥珀酸脱氢酶基因sdh1的重组菌株FPLΔsdh和缺失sdh1基因同时过量表达icl1基因的重组菌株FPLΔsdh-icl。结果表明:3株重组菌的异柠檬酸裂解酶活性由0.33 U/mg分别增加为1.6、5.6和6.6U/mg;而琥珀酸脱氢酶活性则从13.8 U/mg分别降为10.7、0.3和0.3 U/mg。在以木糖为C源的培养基中,3株重组菌生产琥珀酸的能力分别是0.30、1.20和1.60 g/L。     

Genome-scale in silico aided metabolic analysis and flux comparisons of Escherichia coli to improve succinate production

In the post-genome era, it is one challenge to understand the cellular metabolism at the systematic levels. Mathematical modeling of microorganisms and subsequent computer simulation are effective tools for systems biology. In this paper, based on the genome-scale Escherichia coli stoichiometric model iJR904, through the GAMS linear programming package, the in silico maximal succinate yield was estimated to be 1.714 mol/mol glucose. When another two constraints were added, the maximal succinate yield dropped to 1.60 mol/mol glucose. Further analysis substantiated the uniqueness of the flux distribution under such constraints. After comparisons with the metabolic flux analysis (MFA) results computed from the wet experimental data of the three kinds of E. coli, three potential improvement target sites, the glucose phosphotransferase transport system, the pyruvate carboxylase, and the glyoxylate shunt, were identified and selected for the genetic modifications. All the three genetic modified strains showed increased succinate yield. The final strain TUQ19/pQZ6 had a high yield of 1.29 mol succinate/mol glucose and high productivity. The success of the above experiments proved that this in silico optimal succinate production pathway is reasonable and practical. This method may also be used as a general strategy to help enhance the yields of other favorable metabolites in E. coli.     

Determining Actinobacillus succinogenes metabolic pathways and fluxes by NMR and GC-MS analyses of 13C-labeled metabolic product isotopomers

Actinobacillus succinogenes is a promising candidate for industrial succinate production. However, in addition to producing succinate, it also produces formate and acetate. To understand carbon flux distribution to succinate and alternative products we fed A. succinogenes [1-(13)C]glucose and analyzed the resulting isotopomers of excreted organic acids, proteinaceous amino acids, and glycogen monomers by gas chromatography-mass spectrometry and nuclear magnetic resonance spectroscopy. The isotopomer data, together with the glucose consumption and product formation rates and the A. succinogenes biomass composition, were supplied to a metabolic flux model. Oxidative pentose phosphate pathway flux supplied, at most, 20% of the estimated NADPH requirement for cell growth. The model indicated that NADPH was instead produced primarily by the conversion of NADH to NADPH by transhydrogenase and/or by NADP-dependent malic enzyme. Transhydrogenase activity was detected in A. succinogenes cell extracts, as were formate and pyruvate dehydrogenases, which the model suggested were contributing to NADH production. Malic enzyme activity was also detected in cell extracts, consistent with the flux analysis results. Labeling patterns in amino acids and organic acids showed that oxaloacetate and malate were being decarboxylated to pyruvate. These are the first in vivo experiments to show that the partitioning of flux between succinate and alternative fermentation products can occur at multiple nodes in A. succinogenes. The implications for designing effective metabolic engineering strategies to increase A. succinogenes succinate production are discussed.     

Effect of carbon sources differing in oxidation state and transport route on succinate production in metabolically engineered Escherichia coli

In mixed-acid fermentation, succinate synthesis requires one mole of phosphoenolpyruvate (PEP), one mole of CO₂, and two moles of NADH for every mole of succinate to be formed. Different carbon sources with different properties were used to address these requirements. Sorbitol generates one more mole of NADH than glucose. Fermentation of sorbitol was shown in this study (and by others) to produce significantly more succinate than fermentation of glucose, due to increased NADH availability. Xylose fermentation conserves the intracellular PEP pool, since its transport does not require the phosphotransferase system normally used for glucose transport. The extra PEP can then be assimilated in the succinate pathway to improve production. In this study, fermentation of xylose did yield higher succinate production than glucose fermentation. Subsequent inactivation of the acetate and lactate pathways was performed to study metabolite redistribution and the effect on succinate production. With the acetate pathway inactivated, significant carbon flux shifted toward lactate rather than succinate. When both acetate and lactate pathways were inactivated, succinate yield ultimately increased with a concomitant increase in ethanol yield.     

Metabolic evolution of two reducing equivalent-conserving pathways for high-yield succinate production in Escherichia coli

Reducing equivalents are an important cofactor for efficient synthesis of target products. During metabolic evolution to improve succinate production in Escherichia coli strains, two reducing equivalent-conserving pathways were activated to increase succinate yield. The sensitivity of pyruvate dehydrogenase to NADH inhibition was eliminated by three nucleotide mutations in the lpdA gene. Pyruvate dehydrogenase activity increased under anaerobic conditions, which provided additional NADH. The pentose phosphate pathway and transhydrogenase were activated by increased activities of transketolase and soluble transhydrogenase SthA. These data suggest that more carbon flux went through the pentose phosphate pathway, thus leading to production of more reducing equivalent in the form of NADPH, which was then converted to NADH through soluble transhydrogenase for succinate production. Reverse metabolic engineering was further performed in a parent strain, which was not metabolically evolved, to verify the effects of activating these two reducing equivalent-conserving pathways for improving succinate yield. Activating pyruvate dehydrogenase increased succinate yield from 1.12 to 1.31 mol/mol, whereas activating the pentose phosphate pathway and transhydrogenase increased succinate yield from 1.12 to 1.33 mol/mol. Activating these two pathways in combination led to a succinate yield of 1.5 mol/mol (88% of theoretical maximum), suggesting that they exhibited a synergistic effect for improving succinate yield.     

Succinate production in Escherichia coli

Succinate has been recognized as an important platform chemical that can be produced from biomass. While a number of organisms are capable of succinate production naturally, this review focuses on the engineering of Escherichia coli for the production of four-carbon dicarboxylic acid. Important features of a succinate production system are to achieve an optimal balance of reducing equivalents generated by consumption of the feedstock, while maximizing the amount of carbon channeled into the product. Aerobic and anaerobic production strains have been developed and applied to production from glucose and other abundant carbon sources. Metabolic engineering methods and strain evolution have been used and supplemented by the recent application of systems biology and in silico modeling tools to construct optimal production strains. The metabolic capacity of the production strain, the requirement for efficient recovery of succinate, and the reliability of the performance under scaleup are important in the overall process. The costs of the overall biorefinery-compatible process will determine the economic commercialization of succinate and its impact in larger chemical markets.     

Prediction of Rate‐Limiting Reactions for Growth‐Associated Production Using a Constraint‐Based Approach

Identification of a rate‐limiting step in pathways is a key challenge in metabolic engineering. Although the prediction of rate‐limiting steps using a kinetic model is a powerful approach, there are several technical hurdles for developing a kinetic model. In this study, an in silico screening algorithm of key enzyme for metabolic engineering is developed to identify the possible rate‐limiting reactions for the growth‐coupled target production using a stoichiometric model without any experimental data and kinetic parameters. In this method, for each reaction, an upper‐bound flux constraint is imposed and the target production is predicted by linear programming. When the constraint decreases the target production at the optimal growth state, the reaction is thought to be a possible rate‐limiting step. For validation, this method is applied to the production of succinate or 1,4‐butanediol (1,4‐BDO) in Escherichia coli, in which the experimental engineering for eliminating rate‐limiting steps has been previously reported. In succinate production from glycerol, nine reactions including phosphoenolpyruvate carboxylase are predicted as the rate‐limiting steps. In 1,4‐BDO production from glucose, eight reactions including pyruvate dehydrogenase are predicted as the rate‐limiting steps. These predictions include experimentally identified rate‐limiting steps, which would contribute to metabolic engineering as a practical tool for screening candidates of rate‐limiting reactions.     

Succinate production from xylose‐glucose mixtures using a consortium of engineered Escherichia coli

The conversion of variable sugar mixtures into biochemicals poses a challenge for a single microorganism. For example, succinate has not been effectively generated from mixtures of glucose and xylose. In this work, a consortium of two Escherichia coli strains converted xylose and glucose to succinate in a dual phase aerobic/anaerobic process. First, the optimal pathway from xylose or glucose to succinate was determined by expressing either heterologous pyruvate carboxylase or heterologous adenosine triphosphate‐forming phosphoenol pyruvate (PEP) carboxykinase. Expression of PEP carboxykinase (pck) resulted in higher yield (0.86 g/g) and specific productivity (155 mg/gh) for xylose conversion, while expression of pyruvate carboxylase (pyc) resulted in higher productivity (76 mg/gh) for glucose conversion. Then, processes using consortia of the two optimal xylose‐selective and glucose‐selective strains were designed for two different feed ratios of glucose/xylose. In each case the consortia generated over 40 g/L succinate efficiently with yields greater than 0.90 g succinate/g total sugar. This study demonstrates two advantages of microbial consortia for the conversion of sugar mixtures: each sugar‐to‐product pathway can be optimized independently, and the volumetric consumption rate for each sugar can be controlled independently, for example, by altering the biomass concentration of each consortium member strain.     

Respiratory glycerol metabolism of Actinobacillus succinogenes 130Z for succinate production

Actinobacillus succinogenes 130Z naturally produces among the highest levels of succinate from a variety of inexpensive carbon substrates. A few studies have demonstrated that A. succinogenes can anaerobically metabolize glycerol, a waste product of biodiesel manufacture and an inexpensive feedstock, to produce high yields of succinate. However, all these studies were performed in the presence of yeast extract, which largely removes the redox constraints associated with fermenting glycerol, a highly reduced molecule. We demonstrated that A. succinogenes cannot ferment glycerol in minimal medium, but that it can metabolize glycerol by aerobic or anaerobic respiration. These results were expected based on the A. succinogenes genome, which encodes respiratory enzymes, but no pathway for 1,3-propanediol production. We investigated A. succinogenes’s glycerol metabolism in minimal medium in a variety of respiratory conditions by comparing growth, metabolite production, and in vitro activity of terminal oxidoreductases. Nitrate inhibited succinate production by inhibiting fumarate reductase expression. In contrast, growth in the presence of dimethylsulfoxide and in microaerobic conditions allowed high succinate yields. The highest succinate yield was 0.75 mol/mol glycerol (75 % of the maximum theoretical yield) in continuous microaerobic cultures. A. succinogenes could also grow and produce succinate on partially refined glycerols obtained directly from biodiesel manufacture. Finally, by expressing a heterologous 1,3-propanediol synthesis pathway in A. succinogenes, we provide the first proof of concept that A. succinogenes can be engineered to grow fermentatively on glycerol.     

Proposed modifications to metabolic model for glycogen-accumulating organisms under anaerobic conditions

Filipe et al. (2001) proposed an anaerobic metabolic model for glycogen-accumulating organisms (GAO) in which the succinate-propionate pathway was used to describe the production of propionyl-CoA. However, propionyl-CoA is only an intermediate product in the above pathway. Stopping at propionyl-CoA instead of propionate (the end product of the pathway) results in the consumption of one ATP from succinate to succinyl-CoA, which was not accounted for in the model of Filipe et al. (2001). This resulted in significant errors in the stoichiometric coefficients in the final metabolic model. A modified model is presented in this communication and is shown to fit the experimental data significantly better than the original model.     

The ROS Production Induced by a Reverse-Electron Flux at Respiratory-Chain Complex 1 is Hampered by Metformin

Mitochondrial reactive oxygen species (ROS) production was investigated in mitochondria extracted from liver of rats treated with or without metformin, a mild inhibitor of respiratory chain complex 1 used in type 2 diabetes. A high rate of ROS production, fully suppressed by rotenone, was evidenced in non-phosphorylating mitochondria in the presence of succinate as a single complex 2 substrate. This ROS production was substantially lowered by metformin pretreatment and by any decrease in membrane potential (Δ < eqid1 > _m), redox potential (NADH/NAD), or phosphate potential, as induced by malonate, 2,4-dinitrophenol, or ATP synthesis, respectively. ROS production in the presence of glutamate–malate plus succinate was lower than in the presence of succinate alone, but higher than in the presence of glutamate–malate. Moreover, while rotenone both increased and decreased ROS production at complex 1 depending on forward (glutamate–malate) or reverse (succinate) electron flux, no ROS overproduction was evidenced in the forward direction with metformin. Therefore, we propose that reverse electron flux through complex 1 is an alternative pathway, which leads to a specific metformin-sensitive ROS production.     

The succinate receptor GPR91 in neurons has a major role in retinal angiogenesis

Vascularization is essential for tissue development and in restoration of tissue integrity after an ischemic injury. In studies of vascularization, the focus has largely been placed on vascular endothelial growth factor (VEGF), yet other factors may also orchestrate this process. Here we show that succinate accumulates in the hypoxic retina of rodents and, via its cognate receptor G protein-coupled receptor-91 (GPR91), is a potent mediator of vessel growth in the settings of both normal retinal development and proliferative ischemic retinopathy. The effects of GPR91 are mediated by retinal ganglion neurons (RGCs), which, in response to increased succinate levels, regulate the production of numerous angiogenic factors including VEGF. Accordingly, succinate did not have proangiogenic effects in RGC-deficient rats. Our observations show a pathway of metabolite signaling where succinate, acting through GPR91, governs retinal angiogenesis and show the propensity of RGCs to act as sensors of ischemic stress. These findings provide a new therapeutic target for modulating revascularization.     

Metabolic engineering of Escherichia coli for the production of succinate from glycerol

Glycerol has become an ideal feedstock for the microbial production of bio-based chemicals due to its abundance, low cost, and high degree of reduction. We have previously reported the pathways and mechanisms for the utilization of glycerol by Escherichia coli in minimal salts medium under microaerobic conditions. Here we capitalize on such results to engineer E. coli for the production of value-added succinate from glycerol. Through metabolic engineering of E. coli metabolism, succinate production was greatly elevated by (1) blocking pathways for the synthesis of competing by-products lactate, ethanol, and acetate and (2) expressing Lactococcus lactis pyruvate carboxylase to drive the generation of succinate from the pyruvate node (as opposed to that of phosphoenolpyruvate). As such, these metabolic engineering strategies coupled cell growth to succinate production because the synthesis of succinate remained as the primary route of NAD+ regeneration. This feature enabled the operation of the succinate pathway in the absence of selective pressure (e.g. antibiotics). Our biocatalysts demonstrated a maximum specific productivity of ～400 mg succinate/gcell/h and a yield of 0.69 g succinate/g glycerol, on par with the use of glucose as a feedstock.     

一些氨基酸对产甘油假丝酵母甘油生产的促进作用

以EMP途径与TCA循环中间代谢物的添加为对照,研究在尿素为氮源的产甘油假丝酵母发酵过程中添加氨基酸对甘油产量的影响。结果表明:对甘油产量有强促进作用的氨基酸有谷氨酸、谷氨酰胺、天冬氨酸、天冬酰胺、甘氨酸、赖氨酸、酪氨酸、脯氨酸、组氨酸和丝氨酸,其最适添加浓度在0.26～0.45g/L之间,丙酮酸、α_酮戊二酸、草酰乙酸、柠檬酸和琥珀酸的最适添加浓度在0.24～0.42g/L之间;赖氨酸最适于在0h添加,丙酮酸和草酰乙酸在第14h,谷氨酸、谷氨酰胺、组氨酸、脯氨酸、天冬氨酸、酪氨酸、甘氨酸、α_酮戊二酸和琥珀酸在第30h,天冬酰胺、丝氨酸和柠檬酸在第48h;在最适条件下添加这些促进剂,甘油产量均呈显著增加趋势,转化率和增加率分别达到60%和16%以上。氨基酸的作用机理为其脱氨形成的碳骨架经特定的分解代谢途径进入TCA循环,使其强化,导致碳代谢流在3_磷酸甘油醛节点处发生转移,使甘油合成途径的代谢流增加。     

Four different b-type cytochromes in the halophilic archaebacterium, Halobacterium halobium

The halophilic archaebacterium, Halobacterium halobium has been found to contain four different b-type cytochromes. The four components were recognized by their potentiometric characteristics in situ in their functional environment in the membrane of H. halobium. Oxidation-reduction midpoint potentials of these four b-type cytochromes were determined to be +261, +160, +30, and -153 mV, respectively. We also demonstrate that the pathway involved in the transport of reducing equivalents from succinate to oxygen proceeds through the b-type cytochromes with oxidation-reduction midpoint potentials of +261 and +161 mV. The cytochrome with oxidation-reduction midpoint potential of -153 mV was not substrate reducible by NADH but was chemically reducible by dithionite. Antimycin inhibits reduction of b-type cytochrome in the succinate pathway, but has no effect on b-type cytochrome reduction when reducing equivalents are provided by NADH. The carbon monoxide difference spectrum of H. halobium membranes shows at least one carbon monoxide-binding b-type cytochrome, indicating a terminal oxidase. A scheme for electron transport in H.halobium involving the b-type cytochromes and terminal oxidase is suggested.