过量表达烟酸单核苷酸腺苷酰转移酶对大肠杆菌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)的发酵生产丁二酸的潜力菌株。厌氧条件下NADH不能及时再生为NAD+,引起胞内辅酶NAD(H)的不平衡,最终导致厌氧条件下菌株不能利用葡萄糖生长代谢。nadD为催化NAD(H)合成途径中烟酸单核苷酸(NaMN)生成烟酸腺嘌呤二核苷酸(NaAD)的烟酸单核苷酸腺苷酰转移酶(Nicotinic acid mononucleotide adenylyltransferase,NAMNAT)的编码基因,通过过量表达nadD基因能够提高NAD(H)总量与维持合适的NADH/NAD+比例。文中构建了重组菌E.coli NZN111/pTrc99a-nadD,在厌氧摇瓶发酵过程中通过添加终浓度为1.0 mmol/L的IPTG诱导表达,重组菌E.coli NZN111/pTrc99a-nadD中NAD+和NADH的浓度分别比宿主菌E.coli NZN111提高了3.21倍和1.67倍,NAD(H)总量提高了2.63倍,NADH/NAD+从0.64降低为0.41,使重组菌株恢复了厌氧条件下生长和代谢葡萄糖的能力。重组菌与对照菌相比,72 h内可以消耗14.0 g/L的葡萄糖产6.23 g/L的丁二酸,丁二酸产量增加了19倍。     

烟酸转磷酸核糖激酶和丙酮酸羧化酶共表达对大肠杆菌BA002产丁二酸的影响

大肠杆菌BA002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NADH不能及时再生为NAD+,引起胞内辅酶NAD(H)的不平衡,最终导致厌氧条件下菌株不能利用葡萄糖生长代谢。pncB是烟酸转磷酸核糖激酶 (NAPRTase) 的编码基因,通过过量表达pncB基因能够提高NAD(H)总量与维持合适的NADH/NAD+,从而恢复了厌氧条件下重组菌E. coli BA014 (BA002/pTrc99a-pncB) 的生长和产丁二酸的性能。然而,BA014在厌氧发酵过程中有大量丙酮酸积累,为进一步提高菌株的丁二酸生产能力,减少副产物丙酮酸的生成,共表达NAPRTase和来自于乳酸乳球菌 NZ9000中丙酮酸羧化酶 (PYC) 的编码基因pyc,构建了重组菌E. coli BA016 (BA002/pTrc99a-pncB-pyc)。3 L发酵罐结果表明,BA016发酵112 h后,共消耗了35.00 g/L的葡萄糖。发酵结束时,菌体OD600为4.64,产生了25.09 g/L丁二酸。通过共表达pncB和pyc基因,使BA016的丙酮酸积累进一步降低,丁二酸产量进一步提高。     

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     

Increased production of succinic acid in Escherichia coli by overexpression of malate dehydrogenase

Escherichia coli NZN111 is a double mutant with inactivated lactate dehydrogenase and pyruvate formate-lyase. It cannot utilize glucose anaerobically because of its unusually high intracellular NADH/NAD(+) ratio. We have now constructed a recombinant strain, E. coli NZN111/pTrc99a-mdh, which, during anaerobic fermentation, produced 4.3 g succinic acid l(-1) from 13.5 g glucose l(-1). The NADH/NAD(+) ratio decreased from 0.64 to 0.26. Furthermore, dual-phase fermentation (aerobic growth followed by anaerobic phase) resulted in enhanced succinic acid production and reduced byproduct formation. The yield of succinic acid from glucose during the anaerobic phase was 0.72 g g(-1), and the productivity was 1.01 g l(-1) h(-1).     

Effects of overexpression of NAPRTase,NAMNAT, and NAD synthetase in the NAD(H) biosynthetic pathways on the NAD(H) pool,NADH/NAD+ ratio,and succinic acid production with different carbon sources by metabolically engineered Escherichia coli

Escherichia coli BA002, the ldhA and pflB deletion strain, cannot utilize glucose anaerobically due to the inability to regenerate NAD⁺. To regulate NAD(H) pool size and NADH/NAD⁺ ratio, overexpression of the enzymes in the NAD(H) biosynthetic pathways in BA002 was investigated. The results clearly demonstrate that the increased NAD(H) pool size and the decreased NADH/NAD⁺ ratio improved the glucose consumption and cell growth, which improved succinic acid production. When the pncB and the nadD genes were co-overexpressed in CA102, the ratio of NADH/NAD⁺ was decreased from 0.60 to 0.12, and the concentration of NAD(H) was the highest among that of all the strains. Moreover, the dry cell weight (DCW), glucose consumption, and the concentration of succinic acid in CA102 were also the highest. Based on the sufficient NAD⁺ supply after gene modification in the NAD(H) biosynthetic pathways, reductive carbon sources with different amounts of NADH can further change the distribution of metabolites. When sorbitol was used as a carbon source in CA102, the byproducts were lower than those of glucose fermentation, and the yield of succinic acid was increased.     

Combining metabolic engineering and metabolic evolution to develop nonrecombinant strains of Escherichia coli C that produce succinate and malate

Derivatives of Escherichia coli C were engineered to produce primarily succinate or malate in mineral salts media using simple fermentations (anaerobic stirred batch with pH control) without the addition of plasmids or foreign genes. This was done by a combination of gene deletions (genetic engineering) and metabolic evolution with over 2,000 generations of growth-based selection. After deletion of the central anaerobic fermentation genes (ldhA, adhE, ackA), the pathway for malate and succinate production remained as the primary route for the regeneration of NAD+. Under anaerobic conditions, ATP production for growth was obligately coupled to malate dehydrogenase and fumarate reductase by the requirement for NADH oxidation. Selecting strains for improved growth co-selected increased production of these dicarboxylic acids. Additional deletions were introduced as further improvements (focA, pflB, poxB, mgsA). The best succinate biocatalysts, strains KJ060(ldhA, adhE, ackA, focA, pflB) and KJ073(ldhA, adhE, ackA, focA, pflB, mgsA, poxB), produce 622-733 mM of succinate with molar yields of 1.2-1.6 per mole of metabolized glucose. The best malate biocatalyst, strain KJ071(ldhA, adhE, ackA, focA, pflB, mgsA), produced 516 mM malate with molar yields of 1.4 per mole of glucose metabolized.     

Engineering a homobutanol fermentation pathway in Escherichia coli EG03

A homobutanol fermentation pathway was engineered in a derivative of Escherichia coli B (glucose [glycolysis] => 2 pyruvate + 2 NADH; pyruvate [pyruvate dehydrogenase] => acetyl-CoA + NADH; 2 acetyl-CoA [butanol pathway enzymes] + 4 NADH => butanol; summary stoichiometry: glucose => butanol). Initially, the native fermentation pathways were eliminated from E. coli B by deleting the genes encoding for lactate dehydrogenase (ldhA), acetate kinase (ackA), fumarate reductase (frdABCD), pyruvate formate lyase (pflB), and alcohol dehydrogenase (adhE), and the pyruvate dehydrogenase complex (aceEF-lpd) was anaerobically expressed through promoter replacement. The resulting strain, E. coli EG03 (ΔfrdABCD ΔldhA ΔackA ΔpflB Δ adhE ΔpdhR ::pflBp6-aceEF-lpd ΔmgsA), could generate 4 NADH for every glucose oxidized to two acetyl-CoA through glycolysis and the pyruvate dehydrogenase complex. However, EG03 lost its ability for anaerobic growth due to the lack of NADH oxidation pathways. When the butanol pathway genes that encode for acetyl-CoA acetyltransferase (thiL), 3-hydroxybutyryl-CoA dehydrogenase (hbd), crotonase (crt), butyryl-CoA dehydrogenase (bcd, etfA, etfB), and butyraldehyde dehydrogenase (adheII) were cloned from Clostridium acetobutylicum ATCC 824, and expressed in E. coli EG03, a balanced NADH oxidation pathway was established for homobutanol fermentation (glucose => 4 NADH + 2 acetyl-CoA => butanol). This strain was able to convert glucose to butanol (1,254 mg l(-1)) under anaerobic condition.     

Metabolic engineering of Escherichia coli: increase of NADH availability by overexpressing an NAD(+)-dependent formate dehydrogenase

Metabolic engineering studies have generally focused on manipulating enzyme levels through either the amplification, addition, or deletion of a particular pathway. However, with cofactor-dependent production systems, once the enzyme levels are no longer limiting, cofactor availability and the ratio of the reduced to oxidized form of the cofactor can become limiting. Under these situations, cofactor manipulation may become crucial in order to further increase system productivity. Although it is generally known that cofactors play a major role in the production of different fermentation products, their role has not been thoroughly and systematically studied. However, cofactor manipulations can potentially become a powerful tool for metabolic engineering. Nicotinamide adenine dinucleotide (NAD) functions as a cofactor in over 300 oxidation-reduction reactions and regulates various enzymes and genetic processes. The NADH/NAD+ cofactor pair plays a major role in microbial catabolism, in which a carbon source, such as glucose, is oxidized using NAD+ producing reducing equivalents in the form of NADH. It is crucially important for continued cell growth that NADH be oxidized to NAD+ and a redox balance be achieved. Under aerobic growth, oxygen is used as the final electron acceptor. While under anaerobic growth, and in the absence of an alternate oxidizing agent, the regeneration of NAD+ is achieved through fermentation by using NADH to reduce metabolic intermediates. Therefore, an increase in the availability of NADH is expected to have an effect on the metabolic distribution. This paper investigates a genetic means of manipulating the availability of intracellular NADH in vivo by regenerating NADH through the heterologous expression of an NAD(+)-dependent formate dehydrogenase. More specifically, it explores the effect on the metabolic patterns in Escherichia coli under anaerobic and aerobic conditions of substituting the native cofactor-independent formate dehydrogenase (FDH) by and NAD(+)-dependent FDH from Candida boidinii. The over-expression of the NAD(+)-dependent FDH doubled the maximum yield of NADH from 2 to 4 mol NADH/mol glucose consumed, increased the final cell density, and provoked a significant change in the final metabolite concentration pattern both anaerobically and aerobically. Under anaerobic conditions, the production of more reduced metabolites was favored, as evidenced by a dramatic increase in the ethanol-to-acetate ratio. Even more interesting is the observation that during aerobic growth, the increased availability of NADH induced a shift to fermentation even in the presence of oxygen by stimulating pathways that are normally inactive under these conditions.     

The effect of NAPRTase overexpression on the total levels of NAD,the NADH/NAD+ ratio,and the distribution of metabolites in Escherichia coli

Escherichia coli (E. coli) maintains its total NADH/NAD+ intracellular pool by synthesizing NAD through the de novo pathway and the pyridine nucleotide salvage pathway. The salvage pathway recycles intracellular NAD breakdown products and preformed pyridine compounds from the environment, such as nicotinic acid (NA). The enzyme nicotinic acid phosphoribosyltransferase (NAPRTase; EC 2.4.2.11), encoded by the pncB gene, catalyzes the formation of nicotinate mononucleotide (NAMN), a direct precursor of NAD, from NA. This reaction is believed to be the rate-limiting step in the NAD salvage pathway. The current study investigates the effect of overexpressing the pncB gene from Salmonella typhimurium on the total levels of NAD, the NADH/NAD+ ratio, and the production of different metabolites in E. coli under anaerobic chemostat conditions and anaerobic tube experiments. In addition, this paper studies the effect of combining the overexpression of the pncB gene with an NADH regeneration strategy that increases intracellular NADH availability, as we have previously shown. (The effect of increasing NADH availability on the redistribution of metabolic fluxes in Escherichia coli chemostat cultures, Metabolic Eng. 4, 230-237; Metabolic engineering of Escherichia coli: Increase of NADH availability by overexpressing an NAD(+)-dependent formate dehydrogenase, Metabolic Eng. 4, 217-229.) Overexpression of the pncB gene in chemostat experiments increased the total NAD levels, decreased the NADH/NAD+ ratio, and did not significantly redistribute the metabolic fluxes. However, under anaerobic tube conditions, overexpression of the pncB gene led to a significant shift in the metabolic patterns as evidenced by a decrease in lactate production and an increase as high as two-fold in the ethanol-to-acetate (Et/Ac) ratio. These results suggest that under chemostat conditions the total level of NAD is not limiting and the metabolic rates are fixed by the system at steady state. On the other hand, under transient conditions (such as those in batch cultivation) the increase in the total level of NAD can increase the rate of NADH-dependent pathways (ethanol) and therefore change the final distribution of metabolites. The effect of combining overexpression of the pncB gene with the substitution of the native cofactor-independent formate dehydrogenase (FDH) with an NAD(+)-dependent FDH was also investigated under anaerobic tube conditions. This manipulation produced a metabolic pattern that combines a high Et/Ac ratio similar to that obtained with the new FDH with an intermediate lactate level similar to that obtained with the overexpression of the pncB gene. It was found that addition of the pncB gene to the FDH system does not increase further the production of reduced metabolites because the system for NADH regeneration already reached the maximum theoretical yield of approximately 4 mol NADH/mol of glucose.     

The effect of increasing NADH availability on the redistribution of metabolic fluxes in Escherichia coli chemostat cultures

It is generally known that cofactors play a major role in the production of different fermentation products. This paper is part of a systematic study that investigates the potential of cofactor manipulations as a new tool for metabolic engineering. The NADH/NAD+ cofactor pair plays a major role in microbial catabolism, in which a carbon source, such as glucose, is oxidized using NAD+ and producing reducing equivalents in the form of NADH. It is crucially important for continued cell growth that NADH be oxidized to NAD+ and a redox balance be achieved. Under aerobic growth, oxygen is used as the final electron acceptor. While under anaerobic growth, and in the absence of an alternate oxidizing agent, the regeneration of NAD+ is achieved through fermentation by using NADH to reduce metabolic intermediates. Therefore, an increase in the availability of NADH is expected to have an effect on the metabolic distribution. We have previously investigated a genetic means of increasing the availability of intracellular NADH in vivo by regenerating NADH through the heterologous expression of an NAD(+)-dependent formate dehydrogenase and have demonstrated that this manipulation provoked a significant change in the final metabolite concentration pattern both anaerobically and aerobically (Berríos-Rivera et al., 2002, Metabolic engineering of Escherichia coli: increase of NADH availability by overexpressing an NAD(+)-dependent formate dehydrogenase, Metabolic Eng. 4, 217-229). The current work explores further the effect of substituting the native cofactor-independent formate dehydrogenase (FDH) by an NAD(+)-dependent FDH from Candida boidinii on the NAD(H/+) levels, NADH/NAD+ ratio, metabolic fluxes and carbon-mole yields in Escherichia coli under anaerobic chemostat conditions. Overexpression of the NAD(+)-dependent FDH provoked a significant redistribution of both metabolic fluxes and carbon-mole yields. Under anaerobic chemostat conditions, NADH availability increased from 2 to 3 mol NADH/mol glucose consumed and the production of more reduced metabolites was favored, as evidenced by a dramatic increase in the ethanol to acetate ratio and a decrease in the flux to lactate. It was also found that the NADH/NAD+ ratio should not be used as a sole indicator of the oxidation state of the cell. Instead, the metabolic distribution, like the Et/Ac ratio, should also be considered because the turnover of NADH can be fast in an effort to achieve a redox balance.     

Anaerobic synthesis of succinic acid by Escherichia coli strains with activated NAD+ reducing pyruvate dehydrogenase complex

Effect of constitutive expression of the aceEF-lpdA operon genes coding for the enzymes of NAD+ reducing pyruvate dehydrogenase complex on the anaerobic production of succinic acids from glucose by recombinant Escherichia coli strains was studied. Basic producer strains were obtained by inactivation of the main pathways for synthesis of acetic and lactic acids by deletion of the genes ackA, pta, poxB, and ldhA (SGMO.1) in E. coli strain MG 1655 cells and additional introduction of the Bacillus subtilis pyruvate carboxylase (SG M0.1 [pPYC]). A constitutive expression of the genes aceEF-lpdA in derivatives of the basic strains SGM0.1 PL-aceEF-lpdA and SGM0.1 PL-aceEF-lpdA [pPYC] was provided by replacing the native regulatory region of the operon with the lambda phage PL promoter. Molar yields of succinic acid in anaerobic glucose fermentation by strains SGM0.1 P(L)-aceEF-lpdA and SGM0.1 PL-aceEF-lpdA [pPYC] exceeded the corresponding yields displayed by several control strains (exceeded considerably in the case of the strains with a pyruvate carboxylase activity). It is concluded that an increase in the succinic acid production by strain SGM0.1 PL-aceEF-lpdA [pPYC] as compared with the strains SGM0.1 and SGM0.1 [pPYC], which synthesize this substance in the reductive tricarboxylic acid cycle, is determined by activation of the glyoxylate shunt.     

Dihydrolipoamide dehydrogenase mutation alters the NADH sensitivity of pyruvate dehydrogenase complex of Escherichia coli K-12

Under anaerobic growth conditions, an active pyruvate dehydrogenase (PDH) is expected to create a redox imbalance in wild-type Escherichia coli due to increased production of NADH (>2 NADH molecules/glucose molecule) that could lead to growth inhibition. However, the additional NADH produced by PDH can be used for conversion of acetyl coenzyme A into reduced fermentation products, like alcohols, during metabolic engineering of the bacterium. E. coli mutants that produced ethanol as the main fermentation product were recently isolated as derivatives of an ldhA pflB double mutant. In all six mutants tested, the mutation was in the lpd gene encoding dihydrolipoamide dehydrogenase (LPD), a component of PDH. Three of the LPD mutants carried an H322Y mutation (lpd102), while the other mutants carried an E354K mutation (lpd101). Genetic and physiological analysis revealed that the mutation in either allele supported anaerobic growth and homoethanol fermentation in an ldhA pflB double mutant. Enzyme kinetic studies revealed that the LPD(E354K) enzyme was significantly less sensitive to NADH inhibition than the native LPD. This reduced NADH sensitivity of the mutated LPD was translated into lower sensitivity of the appropriate PDH complex to NADH inhibition. The mutated forms of the PDH had a 10-fold-higher K(i) for NADH than the native PDH. The lower sensitivity of PDH to NADH inhibition apparently increased PDH activity in anaerobic E. coli cultures and created the new ethanologenic fermentation pathway in this bacterium. Analogous mutations in the LPD of other bacteria may also significantly influence the growth and physiology of the organisms in a similar fashion.     

共表达烟酸转磷酸核糖激酶和丙酮酸羧化酶对大肠杆菌NZN111产丁二酸的影响

构建了共表达烟酸转磷酸核糖激酶(NAPRTase)和丙酮酸羧化酶(PYC)的重组质粒pTrc99a-pncB-pyc,并考察了重组菌E.coli NZN111/pTrc99a-pncB-pyc生产丁二酸的能力。结果表明:重组菌NZN111/pTrc99a-pncB-pyc的NAPRTase和PYC的比酶活达到最高,分别为20.75和1.04 U/mg,同时,辅酶NADH、NAD+及NAD(H)总量达到最高。厌氧摇瓶发酵结果:48 h能够消耗17.5 g/L的葡萄糖生成14.08 g/L的丁二酸,而丙酮酸的产量大幅度降低,仅为0.11 g/L。本研究为基因工程菌大肠杆菌厌氧条件下发酵生产丁二酸提供了一定的基础。     

Increasing available NADH supply during succinic acid production by Corynebacterium glutamicum

A critical factor in the biotechnological production of succinic acid with Corynebacterium glutamicum is the sufficient supply of NADH. It is conceivable that cofactor availability and the proportion of cofactor in the active form may play an important role in dictating the succinic acid yield. PntAB genes from Escherichia coli can directly catalyze the reversible hydride transfer and adjust the dynamic balance between NADP(H) and NAD(H). Hence, we studied the physiological effect of coenzyme systems by expressing the membrane‐bound transhydrogenase pntAB genes. We have shown experimentally that the pntAB genes could function as an alternative source of NADH. In an anaerobic fermentation with C. glutamicum NC‐3‐pntAB, a 16% higher succinic acid yield and a 57% higher production from glucose were obtained by pntAB expression. Moreover, the formation of by‐products was significantly decreased. The concomitant increase in the consumption of intracellular NADPH from 0.6 to 1.2 mmol/g CDW and the increased NADH/NAD⁺ ratio resulted from introduction of pntAB, suggesting that the membrane‐bound transhydrogenase converted excess NADPH to NADH for succinic acid production. Finally, we explored whether the transhydrogenase had different effects on the succinic acid formation on different carbon sources. The succinic acid yield was increased in the presence of pntAB by 16% on glucose, 7% on sucrose, and without large influence on fructose and xylose. The results of this study demonstrated that the effectiveness of cofactor manipulation could be a promising strategy applied in metabolic engineering. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:12–19, 2015     

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.     

果糖和麦芽糖作为有氧碳源对大肠杆菌NZN111两阶段发酵中厌氧发酵的影响

为了了解磷酸转移酶转运系统 (PTS) 依赖和非PTS依赖代谢的糖类对大肠杆菌生产琥珀酸的影响,进行了两阶段培养,有氧阶段采用PTS依赖型的果糖或非PTS依赖型的麦芽糖作为丙酮酸甲酸裂解酶 (PFL) 和乳酸脱氢酶 (LDH) 双突变株NZN111的碳源,研究其对NZN111厌氧阶段代谢葡萄糖的影响。5 L罐发酵结果表明,以果糖和麦芽糖为碳源有氧培养的细胞恢复了在厌氧条件下快速代谢葡萄糖的能力,琥珀酸和丙酮酸成为主要代谢产物,最终琥珀酸得率分别为0.84和0.75 mol/mol,丙酮酸得率分别达到了0.65和0.83 mol/mol,琥珀酸和丙酮酸终浓度比分别为1.73∶1和1.21∶1。果糖和麦芽糖培养的NZN111与葡萄糖培养的菌体代谢的明显差异推测是cyclic AMP (cAMP) 依赖型和非cAMP依赖型的分解代谢物阻遏调控这两种机制共同作用的结果。     

Doubling the catabolic reducing power (NADH) output of Escherichia coli fermentation for production of reduced products

Homofermentative production of reduced products requires additional reducing power output (NADH) from glucose catabolism. Anaerobic expression of the pyruvate dehydrogenase complex (PDH, encoded by aceEF‐lpd, a normal aerobic operon) is able to provide the additional NADH required for production of reduced products in Escherichia coli fermentation. The multiple promoters (pflBp(1–7)) of pyruvate formate lyase (pflB) were evaluated for anaerobic expression of the aceEF‐lpd operon. Four chromosomal constructs, pflBp(1–7)‐aceEF‐lpd, pflBp(1–6)‐aceEF‐lpd, pflBp(6,7)‐aceEF‐lpd, and pflBp6‐aceEF‐lpd efficiently expressed the PDH complex in anaerobically grown cells. Doubling the reducing power output was achieved when glucose was oxidized to acetyl‐CoA through glycolysis and pyruvate oxidation by the anaerobically expressed PDH complex (glucose →2 acetyl‐CoA + 4 NADH). This additional reducing power output can be used for production of reduced products in anaerobic E. coli fermentation. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Production of succinic acid through overexpression of NAD(+)-dependent malic enzyme in an Escherichia coli mutant.

NAD(+)-dependent malic enzyme was cloned from the Escherichia coli genome by PCR based on the published partial sequence of the gene. The enzyme was overexpressed and purified to near homogeneity in two chromatographic steps and was analyzed kinetically in the forward and reverse directions. The Km values determined in the presence of saturating cofactor and manganese ion were 0.26 mM for malate (physiological direction) and 16 mM for pyruvate (reverse direction). When malic enzyme was induced under appropriate culture conditions in a strain of E. coli that was unable to ferment glucose and accumulated pyruvate, fermentative metabolism of glucose was restored. Succinic acid was the major fermentation product formed. When this fermentation was performed in the presence of hydrogen, the yield of succinic acid increased. The constructed pathway represents an alternative metabolic route for the fermentative production of dicarboxylic acids from renewable feedstocks.     

Genome-based metabolic engineering of Mannheimia succiniciproducens for succinic acid production

Succinic acid is a four-carbon dicarboxylic acid produced as one of the fermentation products of anaerobic metabolism. Based on the complete genome sequence of a capnophilic succinic acid-producing rumen bacterium, Mannheimia succiniciproducens, gene knockout studies were carried out to understand its anaerobic fermentative metabolism and consequently to develop a metabolically engineered strain capable of producing succinic acid without by-product formation. Among three different CO2-fixing metabolic reactions catalyzed by phosphoenolpyruvate (PEP) carboxykinase, PEP carboxylase, and malic enzyme, PEP carboxykinase was the most important for the anaerobic growth of M. succiniciproducens and succinic acid production. Oxaloacetate formed by carboxylation of PEP was found to be converted to succinic acid by three sequential reactions catalyzed by malate dehydrogenase, fumarase, and fumarate reductase. Major metabolic pathways leading to by-product formation were successfully removed by disrupting the ldhA, pflB, pta, and ackA genes. This metabolically engineered LPK7 strain was able to produce 13.4 g/liter of succinic acid from 20 g/liter glucose with little or no formation of acetic, formic, and lactic acids, resulting in a succinic acid yield of 0.97 mol succinic acid per mol glucose. Fed-batch culture of M. succiniciproducens LPK7 with intermittent glucose feeding allowed the production of 52.4 g/liter of succinic acid, with a succinic acid yield of 1.16 mol succinic acid per mol glucose and a succinic acid productivity of 1.8 g/liter/h, which should be useful for industrial production of succinic acid.     

过量表达烟酸转磷酸核糖激酶对大肠杆菌NZN111产丁二酸的影响

大肠杆菌NZN111厌氧发酵的主要产物为丁二酸,是发酵生产丁二酸的潜力菌株。但是由于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),导致辅酶NADH/NAD+不平衡,厌氧条件下不能利用葡萄糖生长代谢。构建烟酸转磷酸核糖激酶的重组菌Escherichia coli NZN111/pTrc99a-pncB,在厌氧摇瓶发酵过程中通过添加0.5 mmol/L的烟酸、0.3 mmol/L的IPTG诱导后重组菌的烟酸转磷酸核糖激酶 (Nicotinic acid phosphor