Effect of flue gas components on succinate production and CO2 fixation by metabolically engineered Escherichia coli

Escherichia coli pfl ldhA ptsG (AFP111) was studied for succinate production in defined medium using trace gases typically found in flue gas; i.e. oxygen (O₂), nitrogen dioxide (NO₂), sulfur dioxide (SO₂) and carbon monoxide (CO). Following aerobic cell growth, cells were exposed to 50% CO₂ and 3–10% O₂, or 50–300 ppm NO₂, SO₂ or CO during the succinate production phase. Although 3% O₂ did not significantly affect succinate formation, 10% O₂ reduced the final succinate concentration from 33 to 17 g/L, specific productivity from 1.90 to 1.13 mmol/g h and yield from 1.15 to 0.81 mol/mol glucose. The effect of O₂ correlated with the culture redox potential (ORP) with more reducing conditions favoring succinate production. The trace gases NO₂ and SO₂ also reduced the rate of succinate formation by as much as 50%, and led to a greater than twofold increase in pyruvate formation. Similar concentrations of CO showed no effect on succinate production rate or yield. Using synthetic flue gas AFP111 generated 12 g/L succinate with a specific productivity of 0.73 mmol/g h and a yield of 0.65 mol/mol.     

pH and base counterion affect succinate production in dual-phase <Emphasis Type="Italic">Escherichia coli</Emphasis> fermentations

Succinate production 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). Two-phase fermentations using a defined medium at several controlled levels of pH were conducted in which an aerobic cell growth phase was followed by an anaerobic succinate production phase using 100% (v/v) CO₂. A pH of 6.4 yielded the highest specific succinate productivity. A metabolic flux analysis at a pH of 6.4 using ¹³C-labeled glucose showed that 61% of the PEP partitioned to oxaloacetate and 39% partitioned to pyruvate, while 93% of the succinate was formed via the reductive arm of the TCA cycle. The flux distribution at a pH of 6.8 was also analyzed and was not significantly different compared to that at a pH of 6.4. Ca(OH)₂ was superior to NaOH or KOH as the base for controlling the pH. By maintaining the pH at 6.4 using 25% (w/v) Ca(OH)₂, the process achieved an average succinate productivity of 1.42 g/l h with a yield of 0.61 g/g.     

Acetate metabolism by Escherichia coli in high-cell-density fermentation.

Little is known about the cellular physiology of Escherichia coli at high cell densities (e.g., greater than 50 g [dry cell weight] per liter), particularly in relation to the cellular response to different growth conditions. E. coli W3100 cultures were grown under identical physical and nutritional conditions, by using a computer-controlled fermentation system which maintains the glucose concentration at 0.5 g/liter, to high cell densities at pH values of 6.0, 6.5, 7.0, and 7.5. The data suggest a relationship between the pH of the environment and the amount of acetate excreted by the organism during growth. At pH values of 6.0 and 6.5, the acetate reached a concentration of 6 g/liter, whereas at pH 7.5, the acetate reached a concentration of 12 g/liter. Furthermore, at pH values of 6.0 to 7.0, the E. coli culture undergoes a dramatic metabolic switch in which oxygen and glucose consumption and CO2 evolution all temporarily decreased by 50 to 80%, with a concomitant initiation of acetate utilization. After a 30-min pause in which approximately 50% of the available acetate is consumed, the culture recovers and resumes consuming glucose and oxygen and producing acetate and CO2 at preswitch levels. During the switch period, the specific activity of isocitrate lyase typically increases approximately fourfold.     

Production of cyclic adenosine monophosphate by Arthrobacter sp. A302 using fed-batch fermentation with pH-shift control

The production of cyclic adenosine monophosphate (cAMP) by Arthrobacter sp. A302 was studied in a 5 L stirred tank fermentor under a range of pH values (6.5–8.0) and glucose feeding rates. In batch fermentation under a controlled pH, the optimum pH for cell growth was 7.5 with dry cell density (X) of 11.43 g L, and the optimum pH for cAMP accumulation was 7.0 with cAMP concentration of 7.41 g L. In order to achieve the high X and cAMP yield simultaneously, a pH-shift control strategy was proposed based on kinetic analysis of specific cell growth rate (μ) and specific cAMP formation rate (q _s ). In this method, pH was controlled to 7.0 for the first 30 h of fermentation, and then subsequently shifted to 7.5 and maintained until the end of the process. Application of this approach significantly enhanced the cAMP concentration. Thereafter, cAMP production was further improved by combining the above-mentioned pH-control system and fed-batch process with glucose at a constant feeding rate of 1.0 g L⁻¹ h⁻¹. Under optimum conditions, the final cAMP production was 10.87 g L, which is 110.0, 46.7, and 27.7% higher than that of the pH-uncontrolled, pH-controlled, and pH-shift controlled methods, respectively.     

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.     

Eliminating side products and increasing succinate yields in engineered strains of Escherichia coli C

Derivatives of Escherichia coli C were previously described for succinate production by combining the deletion of genes that disrupt fermentation pathways for alternative products (ldhA::FRT, adhE::FRT, ackA::FRT, focA-pflB::FRT, mgsA, poxB) with growth-based selection for increased ATP production. The resulting strain, KJ073, produced 1.2 mol of succinate per mol glucose in mineral salts medium with acetate, malate, and pyruvate as significant co-products. KJ073 has been further improved by removing residual recombinase sites (FRT sites) from the chromosomal regions of gene deletion to create a strain devoid of foreign DNA, strain KJ091(DeltaldhA DeltaadhE DeltaackA DeltafocA-pflB DeltamgsA DeltapoxB). KJ091 was further engineered for improvements in succinate production. Deletion of the threonine decarboxylase (tdcD; acetate kinase homologue) and 2-ketobutyrate formate-lyase (tdcE; pyruvate formate-lyase homologue) reduced the acetate level by 50% and increased succinate yield (1.3 mol mol(-1) glucose) by almost 10% as compared to KJ091 and KJ073. Deletion of two genes involved in oxaloacetate metabolism, aspartate aminotransferase (aspC) and the NAD(+)-linked malic enzyme (sfcA) (KJ122) significantly increased succinate yield (1.5 mol mol(-1) glucose), succinate titer (700 mM), and average volumetric productivity (0.9 g L(-1) h(-1)). Residual pyruvate and acetate were substantially reduced by further deletion of pta encoding phosphotransacetylase to produce KJ134 (DeltaldhA DeltaadhE DeltafocA-pflB DeltamgsA DeltapoxB DeltatdcDE DeltacitF DeltaaspC DeltasfcA Deltapta-ackA). Strains KJ122 and KJ134 produced near theoretical yields of succinate during simple, anaerobic, batch fermentations using mineral salts medium. Both may be useful as biocatalysts for the commercial production of succinate.     

Efficient aerobic succinate production from glucose in minimal medium with Corynebacterium glutamicum

Corynebacterium glutamicum, an established industrial amino acid producer, has been genetically modified for efficient succinate production from the renewable carbon source glucose under fully aerobic conditions in minimal medium. The initial deletion of the succinate dehydrogenase genes (sdhCAB) led to an accumulation of 4.7 g l^?1 (40 mM) succinate as well as high amounts of acetate (125 mM) as by‐product. By deleting genes for all known acetate‐producing pathways (pta‐ackA, pqo and cat) acetate production could be strongly reduced by 83% and succinate production increased up to 7.8 g l^?1 (66 mM). Whereas overexpression of the glyoxylate shunt genes (aceA and aceB) or overproduction of the anaplerotic enzyme pyruvate carboxylase (PCx) had only minor effects on succinate production, simultaneous overproduction of pyruvate carboxylase and PEP carboxylase resulted in a strain that produced 9.7 g l^?1 (82 mM) succinate with a specific productivity of 1.60 mmol g (cdw)^?1 h^?1. This value represents the highest productivity among currently described aerobic bacterial succinate producers. Optimization of the production conditions by decoupling succinate production from cell growth using the most advanced producer strain (C. glutamicumΔpqoΔpta‐ackAΔsdhCABΔcat/pAN6‐pyc^P458Sppc) led to an additional increase of the product yield to 0.45 mol succinate mol^?1 glucose and a titre of 10.6 g l^?1 (90 mM) succinate.     

Enhancement of succinate production by metabolically engineered Escherichia coli with co-expression of nicotinic acid phosphoribosyltransferase and pyruvate carboxylase

Escherichia coli BA002, in which the ldhA and pflB genes are deleted, cannot utilize glucose anaerobically due to the inability to regenerate NAD⁺. To restore glucose utilization, overexpression of nicotinic acid phosphoribosyltransferase (NAPRTase) encoded by the pncB gene, a rate-limiting enzyme of NAD(H) synthesis pathway, resulted in a significant increase in cell mass and succinate production under anaerobic conditions. However, a high concentration of pyruvate accumulated. Thus, co-expression of NAPRTase and the heterologous pyruvate carboxylase (PYC) of Lactococcus lactis subsp. cremoris NZ9000 in recombinant E. coli BA016 was investigated. The total concentration of NAD(H) was 9.8-fold higher in BA016 than in BA002, and the NADH/NAD⁺ ratio decreased from 0.60 to 0.04. Under anaerobic conditions, BA016 consumed 17.50 g l^?1 glucose and produced 14.08 g l^?1 succinate with a small quantity of pyruvate. Furthermore, when the reducing agent dithiothreitol or reduced carbon source sorbitol was added, the cell growth and carbon source consumption rate of BA016 was reasonably enhanced and succinate productivity increased.     

产琥珀酸工程菌株的发酵工艺条件优化

对实验室构建的产琥珀酸大肠杆菌工程菌株(E.coliQZ1111)进行发酵工艺条件研究。以AM1低盐培养基为基础,研究不同C、N源及其质量浓度,培养基初始pH和发酵温度等因素对琥珀酸的影响,并在5L发酵罐中进行了补料-分批发酵实验。优化后的发酵条件为葡萄糖20g/L,玉米浆10g/L,pH6.4,发酵温度37℃。在5L发酵罐中培养,琥珀酸产量达到47.9g/L。     

Mitochondria from the hepatopancreas of the marine clam Mercenaria mercenaria: substrate preferences and salt and pH effects on the oxidation of palmitoyl-L-carnitine and succinate

A method is presented for the isolation of mitochondria with good respiratory control from the hepatopancreas of the marine clam Mercenaria mercenaria. Palmitoyl-L-carnitine is the preferred substrate of the mitochondria of the hepatopancreas based on state 3 rates of oxidation (in the presence of ADP). Rates of oxidation of pyruvate and glutamate were about one-half that of the lipid substrate in state 3. alpha-Glycerophosphate was oxidized at a rate about one-third that of palmitoyl-L-carnitine. All Krebs cycle intermediates were oxidized to some extent. Proline was not oxidized at detectable levels. The optimal range of KCl concentrations for the oxidation of palmitoyl-L-carnitine is between 250 and 500 mM whereas the optimal range of KCl concentration for the oxidation of succinate is between 200 and 350 mM. The optimal range of pH for the oxidation of succinate and for the oxidation of palmitoyl-L-carnitine lies between pH 6.5 and 7.5 based on the respiratory control ratio.     

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.     

Antibacterial activity of the metabolic by-products of a Veillonella species and Bacteroides fragilis

A Veillonella species and Bacteroides fragilis were isolated from the cecal contents of adult chickens. When growth on an agar medium supplemented with 0.4% glucose and adjusted to pH 6.5, mixed cultures containing Veillonella and B. fragilis inhibited the growth of Salmonella typhimurium; Salmonella enteritidis, Escherichia coli 0157:H7 and Pseudomonas aeruginosa. Decreasing the glucose concentration of the agar decreased the inhibitory activity of the mixed culture. Mixed cultures grown on agar media supplemented with 0.5% glucose and adjusted to pH 6.5, 7.0 or 7.5 also inhibited the growth of S. typhimurium, S. enteritidis, E. coli 0157:H7 and P. aeruginosa. However, increasing the pH of the agar decreased the inhibitory activity of the mixed culture. Pure cultures of Veillonella or B. fragilis did not inhibit the growth of S. typhimurium, S. enteritidis, E. coli 0157:H7 or P. aeruginosa on any of the agar supplemented with different concentrations of glucose or on any of the agar adjusted to different pH levels. The inhibitory activity of the mixed culture was correlated with the concentration of volatile fatty acids that were formed as B. fragilis metabolized glucose to produce succinate and acetate and as the succinate produced by B. fragilis was decarboxylated by Veillonella to produce propionate.     

Effect of pre-incubation pH on the growth characteristics of Aeromonas hydrophila at 5°C, as assessed by two methods

Two strains of Aeromonas hydrophila (the type strain ATCC 7966 and a food-derived strain JAH4) were pre-incubated at 5°C in Brain Heart Infusion (BHI) broth with pH adjusted to 6.0 or 7.0, and then incubated at the same temperature in BHI broth with pH adjusted to 6.0, 6.5, 7.0 and 7.5. Growth kinetics during incubation were determined by two methods: viable count (VC) and measurement of optical density (O.D.). Pre-incubation at different pH values did not significantly affect the maximum specific growth rates of the strains during incubation, but the lag phases were shorter after pre-incubation at pH 6.0 than at pH 7.0. The VC method was more sensitive than O.D. measurements for assessing lag phase.     

Regulation of reductive production of succinate under anaerobic conditions in baker's yeast

When baker's yeast grown aerobically on ethanol as a carbon source was anaerobically cultured in a medium containing glucose, the activity of a cytoplasmic fumarate reductase irreversibly catalyzing the conversion of fumarate to succinate increased, reaching about 3 times the original activity after 12 h, while the activity of succinate dehydrogenase was almost lost after 10 h. These results indicate that the citrate cycle is partially modified to become a reductive pathway leading to succinate during the anaerobic cultivation. In non-proliferating cells grown anaerobically on glucose, the rates of accumulating succinate and pyruvate were decreased and increased, respectively, with increasing concentrations of L-aspartate or NH4Cl in the medium containing glucose as a substrate. These changes were accompanied with increase in the cellular content of aspartate, an inhibitor of pyruvate carboxylase that is involved in supplying the intermediates of the citrate cycle, and pyruvate, a substrate of the enzyme. The aminotransferase inhibitor, aminooxyacetate, prevented the changes in succinate accumulation and cellular aspartate following the addition of NH4Cl. The addition of L-glutamate caused a marked increase in the rate of succinate accumulation without changing the cellular content of aspartate. Neither L-glutamate nor L-aspartate had the ability to produce succinate. The rate of glucose consumption was not changed upon adding these nitrogen compounds. Similar findings were also observed in experiments using proliferating cells. This report presents evidence that in cells containing a large amount of the fumarate reductase, the production of succinate from glucose is regulated by the cellular level of aspartate through the pyruvate carboxylase reaction and that glutamate regulates the succinate production by a mechanism distinct from that involved in the regulation by L-aspartate.     

一株新型同型产乙酸菌Clostridium sp.的自养和异养生长特性

【背景】同型产乙酸菌是一类利用乙酰辅酶A途径固定CO_2合成自身细胞物质并生成乙酸、乙醇等代谢产物的厌氧菌群,其分布广泛、种类繁多且代谢多样。深入研究同型产乙酸菌菌株的代谢能力及特性,对探索该种群的生理生化特性及其环境作用至关重要。【目的】研究一株同型产乙酸菌Clostridium sp. BXX的最适培养条件及其自养与异养生长特性。【方法】设置BXX菌株培养温度10-55°C、初始pH 6.0-9.0、NaCl浓度0-2.0%、不同氮源,测定菌体细胞含量和产物生成浓度,确定菌株最适培养条件。研究BXX菌株分别以H_2/CO_2、合成气、CO、葡萄糖、1,2-丙二醇、甲酸钠、乙二醇甲醚、甘油、丙酮酸和乳酸为底物时的底物消耗、产物生成、菌体细胞含量和pH等,探究其自养和异养生长特性。【结果】BXX菌株的最适培养温度为30°C,初始pH为7.0,NaCl浓度为1.0%,氮源为酵母粉。BXX菌株能以H2/CO2、合成气、葡萄糖、1,2-丙二醇、甲酸钠、乙二醇甲醚和甘油为底物生长,不能以CO、丙酮酸或乳酸为底物生长。【结论】BXX菌株既能自养生长产乙酸,又能异养生长产乙醇。BXX菌株是乙酸发酵的优良菌种资源,有较好的工业应用潜力。     

Highly efficient conversion of lactate to pyruvate using whole cells of Acinetobacter sp

On an industrial scale, the production of pyruvate at a high concentration from the cheaper lactate substrate is a valuable process. To produce pyruvate from lactate by whole cells, various lactate-utilizing microorganisms were isolated from soil samples. Among them, strain WLIS, identified as Acinetobacter sp., was screened as a pyruvate producer. For the pyruvate preparation from lactate, the preparative conditions were optimized with whole cells of the strain. The cells cultivated in the medium containing 100 mM of l-lactate showed the highest biotransformation efficiency from lactate to pyruvate. The optimized dry-cell concentration, pH, and temperature of reaction were 6 g/L, pH 7.0-7.5, and 30 degrees C, respectively. The influences of ethylenediaminetetraacetic acid (EDTA) and aeration on a biotransformation reaction were carried out under the test conditions. Under the optimized reaction conditions, l-lactate at concentrations of 200 and 500 mM were almost totally stoichiometrically converted into pyruvate in 8 and 12 h, respectively. About 60% of 800 mM of l-lactate was transformed into pyruvate in 24 h. This reduced conversion rate is probably due to the high substrate inhibition in biotransformation.     

Fed-batch culture of a metabolically engineered Escherichia coli strain designed for high-level succinate production and yield under aerobic conditions

An aerobic succinate production system developed by Lin et al. (Metab Eng, in press) is capable of achieving the maximum theoretical succinate yield of 1.0 mol/mol glucose for aerobic conditions. It also exhibits high succinate productivity. This succinate production system is a mutant E. coli strain with five pathways inactivated: DeltasdhAB, Delta(ackA-pta), DeltapoxB, DeltaiclR, and DeltaptsG. The mutant strain also overexpresses Sorghum vulgare pepc. This mutant strain is designated HL27659k(pKK313). Fed-batch reactor experiments were performed for the strain HL27659k(pKK313) under aerobic conditions to determine and demonstrate its capacity for high-level succinate production. Results showed that it could produce 58.3 g/l of succinate in 59 h under complete aerobic conditions. Throughout the entire fermentation the average succinate yield was 0.94+/-0.07 mol/mol glucose, the average productivity was 1.08+/-0.06 g/l-h, and the average specific productivity was 89.77+/-3.40 mg/g-h. Strain HL27659k (pKK313) is, thus, capable of large-scale succinate production under aerobic conditions. The results also showed that the aerobic succinate production system using the designed strain HL27659k(pKK313) is more practical than conventional anaerobic succinate production systems. It has remarkable potential for industrial-scale succinate production and process optimization.     

3-羟基丙酸分批发酵过程中的pH控制策略研究

本文利用重组大肠杆菌以甘油为底物发酵合成3．羟基丙酸,考察了不同pH对3．羟基丙酸产量及菌体生长的影响,发现在pH6．5条件下,细胞比生长速率达到最大值,延迟期也相对较短;而pH7．0有利于3-羟基丙酸的合成,控制pH7．0可以使3-羟基丙酸产量达到7．39g／L。基于不同pH条件下对细胞比生长速率和3-羟基丙酸比生成速率的分析,提出3．羟基丙酸分批发酵过程中的pH控制策略,即在发酵过程前5h将pH控制在6．5,5h～15h控制pH为7．0,此时有利于细胞生长;而后在15h-25h控制pH为7．5,25h后控制pH为7．0,从而使细胞具有较高的3．羟基丙酸比合成速率。在此控制策略下经过34h发酵3-羟基丙酸的终产量达到8．76g／L,比pH7．0条件下的3-羟基丙酸产量提高了18．54％。     

Effect of culture operating conditions on succinate production in a multiphase fed-batch bioreactor using an engineered <Emphasis Type="BoldItalic">Escherichia coli</Emphasis> strain

A metabolically engineered Escherichia coli strain SBS550MG (pHL413) was used in this study to investigate the impact of various culture operating conditions for improving the specific succinate production rate for better final titer while maintaining the theoretical succinate yield on glucose in multiphase fed-batch cultures. Previously, we reported that changes in the level of aeration during the cell growth phase significantly modified gene expression profiles and metabolic fluxes in this system (Martinez et al. 2010). Based on these observations, the examination of culture conditions was mainly focused on the aerobic growth phase. It was found that 2–5 h of low dissolved oxygen culture during the aerobic phase improves cell productivity, but pH control during the aerobic phase was not favorable for the system. Cell viability has been identified as a major limiting factor for succinate production. Supplementing LB medium and betaine, an anti-osmotic stress reagent, did not improve cell activity. A higher succinate titer (537.8 mM) using the current metabolic engineering E. coli strain was achieved, which can potentially be improved further by increasing cell viability.     

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.