Effects of Eliminating Pyruvate Node Pathways and of Coexpression of Heterogeneous Carboxylation Enzymes on Succinate Production by Enterobacter aerogenes

Lowering the pH in bacterium-based succinate fermentation is considered a feasible approach to reduce total production costs. Newly isolated Enterobacter aerogenes strain AJ110637, a rapid carbon source assimilator under weakly acidic (pH 5.0) conditions, was selected as a platform for succinate production. Our previous work showed that the ΔadhE/PCK strain, developed from AJ110637 with inactivated ethanol dehydrogenase and introduced Actinobacillus succinogenes phosphoenolpyruvate carboxykinase (PCK), generated succinate as a major product of anaerobic mixed-acid fermentation from glucose under weakly acidic conditions (pH <6.2). To further improve the production of succinate by the ΔadhE/PCK strain, metabolically engineered strains were designed based on the elimination of pathways that produced undesirable products and the introduction of two carboxylation pathways from phosphoenolpyruvate and pyruvate to oxaloacetate. The highest production of succinate was observed with strain ES04/PCK+PYC, which had inactivated ethanol, lactate, acetate, and 2,3-butanediol pathways and coexpressed PCK and Corynebacterium glutamicum pyruvate carboxylase (PYC). This strain produced succinate from glucose with over 70% yield (gram per gram) without any measurable formation of ethanol, lactate, or 2,3-butanediol under weakly acidic conditions. The impact of lowering the pH from 7.0 to 5.5 on succinate production in this strain was evaluated under pH-controlled batch culture conditions and showed that the lower pH decreased the succinate titer but increased its yield. These findings can be applied to identify additional engineering targets to increase succinate production.     

碳源对琥珀酸放线杆菌发酵产丁二酸的影响及其代谢流量分析

在厌氧条件下, Actinobacillus succinogenes能够利用单糖、双糖和糖醇等碳水化合物发酵生成丁二酸, 其中以山梨醇为碳源时丁二酸的产量最高。代谢流量分析结果表明: 与葡萄糖发酵相比较, 由于代谢系统中积累了更多的NADH, 使得代谢网络关键节点PYR和AcCoA处的代谢流量分配有了较大的变化, 导致更多的碳源流向丁二酸和乙醇, 而乙酸和甲酸的分泌相对减少。     

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。     

Genetic reconstruction of the aerobic central metabolism in Escherichia coli for the absolute aerobic production of succinate

Most reported efforts to enhance production of the industrially valuable specialty chemical succinate have been done under anaerobic conditions, where E. coli undergoes mixed-acid fermentation. These efforts have often been hampered by the limitations of NADH availability, poor cell growth, and slow production. An aerobic succinate production system was strategically designed that allows E. coli to produce and accumulate succinate efficiently and substantially as a product under absolute aerobic conditions. Mutations in the tricarboxylic acid cycle (sdhAB, icd, iclR) and acetate pathways (poxB, ackA-pta) of E. coli were created to construct the glyoxylate cycle for aerobic succinate production. Experiments in flask studies showed that 14.28 mM of succinate could be produced aerobically with a yield of 0.344 mole/mole using 55 mM glucose. In aerobic batch reactor studies, succinate production rate was faster, reaching 0.5 mole/mole in 24 h with a concentration of 22.12 mM; further cultivation showed that succinate production reached 43 mM with a yield of 0.7. There was also substantial pyruvate and TCA cycle C(6) intermediate accumulation in the mutant. The results suggest that more metabolic engineering improvements can be made to this system to make aerobic succinate production more efficient. Nevertheless, this aerobic succinate production system provides the first platform for enhancing succinate production aerobically in E. coli based on the creation of a new aerobic central metabolic network.     

ATP formation associated with fumarate and nitrate reduction in growing cultures of Veillonella alcalescens

Molar growth yields, fermentation balances and enzyme activities were measured in Veillonella alcalescens grown anaerobically with different substrates in the absence or presence of fumarate or nitrate. The molar growth yields on malate (14.3 g dry wt bacteria/mole substrate) and citrate (19.3) were higher than that on lactate (8.6). The molar growth yield on lactate was increased to 15.5 or 19.8 by the addition of fumarate or nitrate, respectively, to the growth medium, and the molar growth yield on citrate was increased to 25.3 by addition of nitrate. Active growth yield was 25.5. From fermentation balances and fermentation systems similar Y_ATP values (g dry wt bacteria/mole ATP) were calculated for all substrates or mixtures of substrates assuming that one mole of ATP is generated at the electron transport from pyruvate, NADH and NADPH to nitrate or fumarate whereas ATP is not produced in the electron transport from lactate to fumarate or nitrate, and, therefore, this assumption was considered to reflect the actual situation. The mean Y_ATP value at a doubling time of 1 h was 16.5 g dry wt bacteria/mole ATP for growth without an added hydrogen acceptor, 14.4 for growth with fumarate, and 14.2 for growth with nitrate.     

产琥珀酸重组大肠杆菌的发酵性能研究

研究了重组大肠杆菌JM001(△ppc)/pTrc99a-pck发酵产琥珀酸的性能,结果表明厌氧条件下其耗糖能力和产酸能力分别为对照菌株JM001的4.2倍和15.3倍。进一步优化发酵条件表明：采用接入菌泥的发酵方式比按照10%接种量转接厌氧发酵的效果要好,琥珀酸的对葡萄糖的质量收率提高了约10%,且副产物乙酸的量进一步降低。初始葡萄糖浓度高于60g/L时会对菌株的生长和产酸产生抑制,且浓度越高,抑制作用越明显。7L发酵罐放大实验中,整个厌氧发酵阶段葡萄糖的消耗速率为0.42g/(L.h),琥珀酸对葡萄糖的质量收率为67.75%,琥珀酸的生产强度为0.28g/(L.h)。     

过量表达苹果酸脱氢酶对大肠杆菌NZN111产丁二酸的影响

大肠杆菌NZN111是敲除了乳酸脱氢酶的编码基因 (ldhA) 和丙酮酸-甲酸裂解酶的编码基因 (pflB) 的工程菌,厌氧条件下由于辅酶NAD(H) 的不平衡导致其丧失了代谢葡萄糖的能力。构建了苹果酸脱氢酶的重组菌大肠杆菌NZN111/pTrc99a-mdh,在厌氧摇瓶发酵过程中通过0.3 mmol/L的IPTG诱导后重组菌的苹果酸脱氢酶 (Malate dehydrogenase,MDH) 酶活较出发菌株提高了14.8倍,NADH/NAD+的比例从0.64下降到0.26,同时NAD+和NADH浓度分别     

Metabolic engineering to improve ethanol production in Thermoanaerobacter mathranii

Thermoanaerobacter mathranii can produce ethanol from lignocellulosic biomass at high temperatures, but its biotechnological exploitation will require metabolic engineering to increase its ethanol yield. With a cofactor-dependent ethanol production pathway in T. mathranii, it may become crucial to regenerate cofactor to increase the ethanol yield. Feeding the cells with a more reduced carbon source, such as mannitol, was shown to increase ethanol yield beyond that obtained with glucose and xylose. The ldh gene coding for lactate dehydrogenase was previously deleted from T. mathranii to eliminate an NADH oxidation pathway. To further facilitate NADH regeneration used for ethanol formation, a heterologous gene gldA encoding an NAD⁺-dependent glycerol dehydrogenase was expressed in T. mathranii. One of the resulting recombinant strains, T. mathranii BG1G1 (Δldh, P _xyl GldA), showed increased ethanol yield in the presence of glycerol using xylose as a substrate. With an inactivated lactate pathway and expressed glycerol dehydrogenase activity, the metabolism of the cells was shifted toward the production of ethanol over acetate, hence restoring the redox balance. It was also shown that strain BG1G1 acquired the capability to utilize glycerol as an extra carbon source in the presence of xylose, and utilization of the more reduced substrate glycerol resulted in a higher ethanol yield.     

Influence of Metronidazole, CO, CO2, and Methanogens on the Fermentative Metabolism of the Anaerobic Fungus Neocallimastix sp. Strain L2

The effects of metronidazole, CO, methanogens, and CO₂ on the fermentation of glucose by the anaerobic fungus Neocallimastix sp. strain L2 were investigated. Both metronidazole and CO caused a shift in the fermentation products from predominantly H₂, acetate, and formate to lactate as the major product and caused a lower glucose consumption rate and cell protein yield. An increased lactate dehydrogenase activity and a decreased hydrogenase activity were observed in cells grown under both culture conditions. In metronidazole-grown cells, the amount of hydrogenase protein was decreased compared with the amount in cells grown in the absence of metronidazole. When Neocallimastix sp. strain L2 was cocultured with the methanogenic bacterium Methanobrevibacter smithii, the fermentation pattern changed in the opposite direction: H₂ and acetate production increased at the expense of the electron sink products lactate, succinate, and ethanol. A concomitant decrease in the enzyme activities leading to these electron sink products was observed, as well as an increase in the glucose consumption rate and cell protein yield, compared with those of pure cultures of the fungus. Low levels of CO₂ in the gas phase resulted in increased H₂ and lactate formation and decreased production of formate, acetate, succinate, and ethanol, a decreased glucose consumption rate and cell protein yield, and a decrease in most of the hydrogenosomal enzyme activities. None of the tested culture conditions resulted in changed quantities of hydrogenosomal proteins. The results indicate that manipulation of the pattern of fermentation in Neocallimastix sp. strain L2 results in changes in enzyme activities but not in the proliferation or disappearance of hydrogenosomes.     

Improvement of the redox balance increases L-valine production by Corynebacterium glutamicum under oxygen deprivation conditions

Production of L-valine under oxygen deprivation conditions by Corynebacterium glutamicum lacking the lactate dehydrogenase gene ldhA and overexpressing the L-valine biosynthesis genes ilvBNCDE was repressed. This was attributed to imbalanced cofactor production and consumption in the overall L-valine synthesis pathway: two moles of NADH was generated and two moles of NADPH was consumed per mole of L-valine produced from one mole of glucose. In order to solve this cofactor imbalance, the coenzyme requirement for L-valine synthesis was converted from NADPH to NADH via modification of acetohydroxy acid isomeroreductase encoded by ilvC and introduction of Lysinibacillus sphaericus leucine dehydrogenase in place of endogenous transaminase B, encoded by ilvE. The intracellular NADH/NAD(+) ratio significantly decreased, and glucose consumption and L-valine production drastically improved. Moreover, L-valine yield increased and succinate formation decreased concomitantly with the decreased intracellular redox state. These observations suggest that the intracellular NADH/NAD(+) ratio, i.e., reoxidation of NADH, is the primary rate-limiting factor for L-valine production under oxygen deprivation conditions. The L-valine productivity and yield were even better and by-products derived from pyruvate further decreased as a result of a feedback resistance-inducing mutation in the acetohydroxy acid synthase encoded by ilvBN. The resultant strain produced 1,470 mM L-valine after 24 h with a yield of 0.63 mol mol of glucose(-1), and the L-valine productivity reached 1,940 mM after 48 h.     

Efficient succinic acid production from glucose through overexpression of pyruvate carboxylase in an Escherichia coli alcohol dehydrogenase and lactate dehydrogenase mutant

An adhE, ldhA double mutant Escherichia coli strain, SBS110MG, has been constructed to produce succinic acid in the presence of heterologous pyruvate carboxylase (PYC). The strategic design aims at diverting maximum quantities of NADH for succinate synthesis by inactivation of NADH competing pathways to increase succinate yield and productivity. Additionally an operational PFL enzyme allows formation of acetyl-CoA for biosynthesis and formate as a potential source of reducing equivalents. Furthermore, PYC diverts pyruvate toward OAA to favor succinate generation. SBS110MG harboring plasmid pHL413, which encodes the heterologous pyruvate carboxylase from Lactococcus lactis, produced 15.6 g/L (132 mM) of succinate from 18.7 g/L (104 mM) of glucose after 24 h of culture in an atmosphere of CO(2) yielding 1.3 mol of succinate per mole of glucose. This molar yield exceeded the maximum theoretical yield of succinate that can be achieved from glucose (1 mol/mol) under anaerobic conditions in terms of NADH balance. The current work further explores the importance of the presence of formate as a source of reducing equivalents in SBS110MG(pHL413). Inactivation of the native formate dehydrogenase pathway (FDH) in this strain significantly reduced succinate yield, suggesting that reducing power was lost in the form of formate. Additionally we investigated the effect of ptsG inactivation in SBS110MG(pHL413) to evaluate the possibility of a further increase in succinate yield. Elimination of the ptsG system increased the succinate yield to 1.4 mol/mol at the expense of a reduction in glucose consumption of 33%. In the presence of PYC and an efficient conversion of glucose to products, the ptsG mutation is not indispensable since PEP converted to pyruvate as a result of glucose phosphorylation by the glucose specific PTS permease EIICB(glu) can be rediverted toward OAA favoring succinate production.     

碳源对重组大肠杆菌两阶段发酵产丁二酸的影响

研究了在好氧培养基中分别添加不同碳源对两阶段发酵菌体生长、酶活及代谢产物分布的影响,结果表明添加4mmol/L葡萄糖和12,54,80mmol/L乙酸钠均可以提高好氧阶段的菌体密度和相关酶活。将不同条件下培养的菌体转接厌氧发酵后,厌氧阶段的酶活和代谢产物分布也发生改变。进一步对酶活及代谢产物分析表明：Escherichia coli NZN111(sfcA)厌氧发酵过程中,磷酸烯醇式丙酮酸羧化激酶(PCK)是产丁二酸的关键酶,丙酮酸激酶(PYK)主要和副产物丙酮酸的积累有关,异柠檬酸裂解酶(ICL)对丁二酸产量也有一定影响。好氧培养基中添加80mmol/L乙酸钠,厌氧发酵结束时丁二酸的质量收率可达89.0%,相比对照提高了16.6%。     

Formation of formate and hydrogen, and flux of reducing equivalents and carbon in Ruminococcus flavefaciens Fd-1

A pathway for conversion of the metabolic intermediate phosphoenolpyruvate (PEP) and the formation of acetate, succinate, formate, and H₂ in the anaerobic cellulolytic bacterium Ruminococcus flavefaciens FD-1 was constructed on the basis of enzyme activities detected in extracts of cells grown in cellulose- or cellobiose-limited continuous culture. PEP was converted to acetate and CO₂ (via pyruvate kinase, pyruvate dehydrogenase, and acetate kinase) or carboxylated to form succinate (via PEP carboxykinase, malate dehydrogenase, fumarase, and fumarate reductase). Lactate was not formed even during rapid growth (batch culture, µ = 0.35/h). H₂ was formed by a hydrogenase rather than by cleavage of formate, and ¹³C-NMR and¹⁴ C-exchange reaction data indicated that formate was produced by CO₂ reduction, not by a cleavage of pyruvate. The distribution of PEP into the acetate and succinate pathways was not affected by changing extracellular pH and growth rates within the normal growth range. However, increasing growth rate from 0.017/h to 0.244/h resulted in a shift toward formate production, presumably at the presence of H₂. This shift suggested that reducing equivalents could be balanced through formate or H₂ production without affecting the yields of the major carbon-containing fermentation endproducts.     

Improved Production of 2,3-Butanediol in Bacillus amyloliquefaciens by Over-Expression of Glyceraldehyde-3-Phosphate Dehydrogenase and 2,3-butanediol Dehydrogenase

Background

Previously, a safe strain, Bacillus amyloliquefaciens B10-127 was identified as an excellent candidate for industrial-scale microbial fermentation of 2,3-butanediol (2,3-BD). However, B. amyloliquefaciens fermentation yields large quantities of acetoin, lactate and succinate as by-products, and the 2,3-BD yield remains prohibitively low for commercial production.

Methodology/Principal Findings

In the 2,3-butanediol metabolic pathway, glyceraldehyde-3-phosphate dehydrogenase (GAPDH) catalyzes the conversion of 3-phosphate glyceraldehyde to 1,3-bisphosphoglycerate, with concomitant reduction of NAD⁺ to NADH. In the same pathway, 2,3-BD dehydrogenase (BDH) catalyzes the conversion of acetoin to 2,3-BD with concomitant oxidation of NADH to NAD⁺. In this study, to improve 2,3-BD production, we first over-produced NAD⁺-dependent GAPDH and NADH-dependent BDH in B. amyloliquefaciens. Excess GAPDH reduced the fermentation time, increased the 2,3-BD yield by 12.7%, and decreased the acetoin titer by 44.3%. However, the process also enhanced lactate and succinate production. Excess BDH increased the 2,3-BD yield by 16.6% while decreasing acetoin, lactate and succinate production, but prolonged the fermentation time. When BDH and GAPDH were co-overproduced in B. amyloliquefaciens, the fermentation time was reduced. Furthermore, in the NADH-dependent pathways, the molar yield of 2,3-BD was increased by 22.7%, while those of acetoin, lactate and succinate were reduced by 80.8%, 33.3% and 39.5%, relative to the parent strain. In fed-batch fermentations, the 2,3-BD concentration was maximized at 132.9 g/l after 45 h, with a productivity of 2.95 g/l·h.

Conclusions/Significance

Co-overexpression of bdh and gapA genes proved an effective method for enhancing 2,3-BD production and inhibiting the accumulation of unwanted by-products (acetoin, lactate and succinate). To our knowledge, we have attained the highest 2,3-BD fermentation yield thus far reported for safe microorganisms.     

Effect of CO2 on succinate production in dual-phase Escherichia coli fermentations

Succinate production under different concentrations of carbon dioxide (CO₂) was studied in Escherichia coli AFP111, which contains mutations in pyruvate formate lyase (pfl), lactate dehydrogenase (ldhA) and the phosphotransferase system glucosephosphotransferase enzyme II (ptsG). A series of two-phase fermentations were conducted in which an aerobic cell growth phase was followed by an anaerobic succinate production phase using several constant concentrations of CO₂. As the concentration of CO₂ in the gas phase increased from 0% to 50%, the succinate specific productivity increased from 1.9 mg/g h to 225 mg/g h, and the succinate yield increased from 0.04 g/g to 0.75 g/g. Above 50% CO₂, succinate production did not increase further. Intracellular fluxes were determined at three different CO₂ concentrations (3%, 10%, and 50%) using ¹³C-label tracing coupled with LC–MS analysis. The fraction of carbon flux into the pentose phosphate pathway increased from 0.04 at 3% CO₂ to 0.17 at 50% CO₂. Also, the fractional flux through anaplerotic carboxylation at the phosphoenolpyruvate (PEP) node increased slightly from 0.53 at 3% CO₂ to 0.63 at 50% CO₂. The increased flux into the pentose phosphate pathway is attributed to an increased demand for reduced cofactors with elevated CO₂. A four-process explicit model to describe the CO₂ transfer and utilization was proposed. The model predicted that at CO₂ concentrations below about 30–40% the system becomes limited by gas phase CO₂, while at higher CO₂ concentrations the system is limited by PEP carboxylase enzyme kinetics.     

Metabolic control of Clostridium thermocellum via inhibition of hydrogenase activity and the glucose transport rate

Clostridium thermocellum has the ability to catabolize cellulosic biomass into ethanol, but acetic acid, lactic acid, carbon dioxide, and hydrogen gas (H₂) are also produced. The effect of hydrogenase inhibitors (H₂, carbon monoxide (CO), and methyl viologen) on product selectivity was investigated. The anticipated effect of these hydrogenase inhibitors was to decrease acetate production. However, shifts to ethanol and lactate production are also observed as a function of cultivation conditions. When the sparge gas of cellobiose-limited chemostat cultures was switched from N₂ to H₂, acetate declined, and ethanol production increased 350%. In resting cell suspensions, lactate increased when H₂ or CO was the inhibitor or when the cells were held at elevated hyperbaric pressure (6.8 atm). In contrast, methyl-viologen-treated resting cells produced twice as much ethanol as the other treatments. The relationship of chemostat physiology to methyl viologen inhibition was revealed by glucose transport experiments, in which methyl viologen decreased the rate of glucose transport by 90%. C. thermocellum produces NAD⁺ from NADH by H₂, lactate, and ethanol production. When the hydrogenases were inhibited, the latter two products increased. However, excess substrate availability causes fructose 1,6-diphosphate, the glycolytic intermediate that triggers lactate production, to increase. Compensatory ethanol production was observed when the chemostat fluid dilution rate or methyl viologen decreased substrate transport. This research highlights the complex effects of high concentrations of dissolved gases in fermentation, which are increasingly envisioned in microbial applications of H₂ production for the conversion of synthetic gases to chemicals.     

Pyruvate metabolism in Helicobacter pylori

The metabolism of pyruvate by Helicobacter pylori was investigated employing one- and two-dimensional ¹H and ¹³C nuclear magnetic resonance spectroscopy. Generation of pyruvate from l-serine in incubations with whole cell lysates indicated the presence of serine dehydratase activity in the bacterium. Pyruvate was formed also in cell suspensions and lysates from phosphoenol pyruvate. Metabolically competent cells incubated aerobically with pyruvate yielded alanine, lactate, acetate, formate, and succinate. The production of alanine and lactate indicated the presence of alanine transaminase and lactate dehydrogenase activities, respectively. Accumulation of acetate and formate as metabolic products provided evidence for the existence of a mixed-acid fermentation pathway in the microorganism. Formation of succinate suggested the incorporation of the pyruvate carbon skeleton into the Kreb's cycle. Addition of pyruvate to various liquid culture media did not affect bacterial growth or loss of viability. The variety of products formed using pyruvate as the sole substrate showed the important role of this metabolite in the energy metabolism of H. pylori.     

Energetics of glucose uptake in Salmonella typhimurium

We have studied the energetics of glucose uptake in Salmonella typhimurium. Strain PP418 transprots glucose via the phosphoenolpyruvate: glucose phosphotransferase system, while strain PP1705 lacks this system and can only use the galactose permease for glucose uptake. These two strains were cultured anaerobically in glucose-limited chemostats. Both strains produced ethanol and acetate in equimolar amounts but a significant difference was observed in the molar growth yield on glucose (Y _Glc). It is suggested that this difference is due to a difference in the energetics of the glucose uptake systems in the two strains.Assuming an equal Y _ATP for both strains, we could calculate that uptake of 1 mole of glucose via the galactose permease consumes the equivalent of 0.5 mole of ATP. With the additional assumption that one proton is transported in symport with one glucose molecule, these results imply a stoichiometry of two protons per ATP hydrolysed.Abbreviations PTS Phosphoenolpyruvate: carbohydrate phosphotransferase system - D dilution rate (h^-1 - DW dry weight - GalP galactose permease - EtOH ethanol - HAc acetate - Lact lactate - Suc succinate - HFo formate - Glc Glucose - Y _Glc, Y _ATP yield of cells per glucose or ATP - q specific production rate