Intracellular Accumulation of the Monomeric Precursors of Polyphosphates and Polyhydroxyalkanoates in Acinetobacter calcoaceticusand Escherichia coliCells

The formation of polyhydroxyalkanoates granules in anaerobically grown Escherichia coliM-17 cells was found to be preceded by the intracellular accumulation of carbonic acids (predominantly, acetic acid), amounting to 9% of the cytosol. The intracellular concentration of acidic metabolites increased after the lyophilization of the bacterial biomass and decreased after its long-term storage (3.5–13.5 years). The decrease in the concentration of acidic metabolites is likely due to the dehydration of dimeric carbonic acids in the viscoelastic cytosol of resting bacterial cells. The hydrophobic obligately aerobic cells of Acinetobacter calcoaceticusIEGM 549 are able to utilize a wide range of growth substrates (from acetate and citrate to hydrophobic hydrocarbons), which is considerably wider than the range of the growth substrates of E. coli(predominantly, carbohydrates). The minimal essential and optimal concentrations of orthophosphates in the growth medium of A. calcoaceticuswere found to be tens of times lower than in the case of E. coli.The intracellular content of orthophosphates in A. calcoaceticuscells reached 35–77% of the total phosphorus content (P_total), providing for the intense synthesis of polyphosphates. The P_totalof the A. calcoaceticuscells grown in media with different proportions between the concentrations of acetate and phosphorus varied from 0.7 to 3.3%, averaging 2%. This value of P_totalis about two times higher than that observed for fermenting E. colicells. Lowering the cultivation temperature of A. calcoaceticusfrom 37–32 to 4°C augmented the accumulation of orthophosphates in the cytoplasm, presumably owing to a decreased requirement of growth processes for orthophosphate. In this case, if the concentration of phosphates in the cultivation medium was low, they were completely depleted.     

Disruption of glpF gene encoding the glycerol facilitator improves 1,3-propanediol production from glucose via glycerol in Escherichia coli

Engineered Escherichia coli has recently been applied to produce 1,3-propanediol (1,3-PDO) from glucose. A metabolic intermediate in the production pathway, glycerol, is partially secreted into the extracellular of E. coli through a glycerol facilitator encoded by glpF, and this secretion consequently decreases 1,3-PDO production. Therefore, we aimed to determine whether disrupting the glpF gene would improve 1,3-PDO production in E. coli. The intracellular glycerol concentration in a glpF-disruptant was 7·5 times higher than in a non-disruptant. The glpF-disrupted and non-disrupted E. coli strains produced 0·26 and 0·09 g l⁻¹ of 1,3-PDO, respectively, from 1% glucose after 72 h of cultivation. The specific growth rate (μ) and the 1,3-PDO yield from glucose (Y_P/S) in the disruptant were higher than those in the non-disruptant (ΔglpF, μ = 0·08 ± 0·00 h⁻¹, Y_P/S = 0·06 mol mol-glucose⁻¹; BW25113, μ = 0·06 ± 0·00 h⁻¹, Y_P/S = 0·02 mol mol-glucose⁻¹). Disruption of the glpF gene decreased the production of the by-product, acetic acid. These results indicated that disruption of glpF increased the intracellular concentration of glycerol and consequently increased 1,3-PDO production in E. coli.     

Development and characterization of a potent producer of penicillin G amidase by mutagenization

Summary The penicillin G amidase (PGA) activity of a parent strain of E. coli (PCSIR-102) was enhanced by chemical mutagenization with N-methyl-N′-nitro-N-nitrosoguanidine (MNNG). After screening and optimization, a penicillinase deficient mutant (MNNG-37) was isolated and found effective for the production of penicillin G amidase as compared to the parent strain of E. coli (PCSIR-102). Penicillin G amidase activity of MNNG-37 appeared during an early stage of growth, whereas PCSIR-102 did not exhibit PGA activity due to the presence of penicillinase enzyme which inhibits the activity of enzyme PGA. However, MNNG-37 gave a three-fold increase in enzyme activity (231 IU mg⁻¹) as compared to PCSIR-102 (77 IU mg⁻¹) in medium containing 0.15 and 0.1% concentrations of phenylacetic acid, respectively which was added after 6 h of cultivation. The difference in K _m values of the enzyme produced by parent strain PCSIR-102 (0.26 mM) and mutant strain MNNG-37 (0.20 mM) is significant (1.3-fold increase in K _m value) which may show the superiority of the latter in terms of better enzyme properties.     

Influence of temperature on the production of an archaeal thermoactive alcohol dehydrogenase from Pyrococcus furiosus with recombinant Escherichia coli

The heterologous production of a thermoactive alcohol dehydrogenase (AdhC) from Pyrococcus furiosus in Escherichia coli was investigated. E. coli was grown in a fed-batch bioreactor in minimal medium to high cell densities (cell dry weight 76 g/l, OD₆₀₀ of 150). Different cultivation strategies were applied to optimize the production of active AdhC, such as lowering the cultivation temperature from 37 to 28°C, heat shock of the culture from 37 to 42°C and from 37 to 45°C, and variation of time of induction (induction at an OD₆₀₀ of 40, 80 and 120). In addition to the production of active intracellular protein, inclusion bodies were always observed. The maximal activity of 30 U/l (corresponding to 6 mg/l active protein) was obtained after a heat shock from 37 to 42°C, and IPTG induction of the adhC expression at an OD₆₀₀ of 120. Although no general rules can be provided, some of the here presented variations may be applicable for the optimization of the heterologous production of proteins in general, and of thermozymes in particular.     

调控大肠杆菌胞内ATP和NADH水平促进琥珀酸生产

琥珀酸作为一种重要的C4平台化合物,广泛应用于食品、化学、医药等领域。利用大肠杆菌(Escherichia coli)发酵生产琥珀酸受胞内辅因子不平衡的影响,存在产率低、生产强度低、副产物多等问题。为此,对不同氧气条件下琥珀酸产量和化学计量学分析发现,微厌氧条件下E.coli FMME-N-26高效积累琥珀酸需要借助三羧酸循环(tricarboxylic acid cycle,TCA)为还原性三羧酸途径(reductive tricarboxylic acid pathway,r-TCA)提供足够的ATP和NADH。通过减少ATP消耗、强化ATP合成、阻断NADH竞争途径和构建NADH回补路径等代谢工程策略,组合调控胞内ATP与NADH含量,获得工程菌株E.coli FW-17。通过发酵条件优化,菌株E.coli FW-17在5 L发酵罐能积累139.52 g/L琥珀酸,比出发菌株提高了17.81%,乙酸浓度为1.40 g/L,降低了67.59%。进一步在1000 L发酵罐中进行放大实验,琥珀酸产量和乙酸浓度分别为140.2 g/L和1.38 g/L。     

Galactose induces the expression of penicillin acylase under control of the lac promoter in recombinant Escherichia coli

The expression of penicillin acylase (PA), cloned in the pPA102 plasmid under control of the wild-type lac promoter and using galactose as inducer in Escherichia coli JM101, JM103 and JM105 transformant cells, was analyzed. The E. coli JM101/pPA102 cultures attained the highest specific activity of PA. For large scale PA production based on E. coli JM101/pPA102 a culture media with galactose instead of isopropyl-thio-galactopyranoside as inducer would be as successful and less expensive.     

Quantitative aspects of glucose metabolism by Escherichia coli B/r,grown in the presence of pyrroloquinoline quinone

Escherichia coli B/r was grown in chemostat cultures under various limitations with glucose as carbon source. Since E. coli only synthesized the glucose dehydrogenase (GDH) apo-enzyme and not the appropriate cofactor, pyrroloquinoline quinone (PQQ), no gluconate production could be observed. However, when cell-saturating amounts of PQQ (nmol to mol range) were pulsed into steady state glucose-excess cultures of E. coli, the organisms responded with an instantaneous formation of gluconate and an increased oxygen consumption rate. This showed that reconstitution of GDH in situ was possible.Hence, in order to examine the influence on glucose metabolism of an active GDH, E. coli was grown aerobically in chemostat cultures under various limitations in the presence of PQQ. It was found that the presence of PQQ indeed had a sizable effect: at pH 5.5 under phosphate- or sulphate- limited conditions more than 60% of the glucose consumed was converted to gluconate, which resulted in steady state gluconate concentrations up to 80 mmol/l. The specific rate of gluconate production (0.3–7.6 mmol·h^-1·(g dry wt cells)^-1) was dependent on the growth rate and the nature of the limitation. The production rate of other overflow metabolites such as acetate, pyruvate, and 2-oxoglutarate, was only slightly altered in the presence of PQQ. The fact that the cells were now able to use an active GDH apparently did not affect apo-enzyme synthesis.Abbreviations HEPES N-2-hydroxy-ethylpiperazine-N-2-ethane sulphonic acid - MES 2-morpholinoethane sulphonic acid - PQQ pyrroloquinoline quinone (systematic name: 2,7,9-tricarboxy-1H-pyrrolo-(2,3-f)-quinoline-4,5-dione) - WB Wurster's Blue (systematic name: 1,4-bis-(dimethylamino)-benzene perchlorate     

Over-expression of glucose dehydrogenase improves cell growth and riboflavin production in Bacillus subtilis

Ribulose 5-phosphate is a precursor for riboflavin biosynthesis. Alteration of carbon flow into the pentose phosphate pathway will affect the availability of ribulose 5-phosphate and the riboflavin yield. We have modulated carbon flow in Bacillus subtilis through the gluconate bypass by over-expression of glucose dehydrogenase under the control of the constitutively expressed P43 promoter. Over-expression of glucose dehydrogenase resulted in low acid production (acetate and pyruvate). The substantial reduction in acid production is accompanied by increased riboflavin production and an increased rate of growth while glucose consumption remained unchanged. Metabolic analysis indicated that over-expression of glucose dehydrogenase increased intracellular pool of ribulose 5-phosphate. The high concentrations of ribulose 5-phosphate could explain the increased riboflavin production.     

Metabolic engineering of E. coli for improving mevalonate production to promote NADPH regeneration and enhance acetyl-CoA supply

Microbial production of mevalonate from renewable feedstock is a promising and sustainable approach for the production of value-added chemicals. We describe the metabolic engineering of Escherichia coli to enhance mevalonate production from glucose and cellobiose. First, the mevalonate-producing pathway was introduced into E. coli and the expression of the gene atoB, which encodes the gene for acetoacetyl-CoA synthetase, was increased. Then, the deletion of the pgi gene, which encodes phosphoglucose isomerase, increased the NADPH/NADP⁺ ratio in the cells but did not improve mevalonate production. Alternatively, to reduce flux toward the tricarboxylic acid cycle, gltA, which encodes citrate synthetase, was disrupted. The resultant strain, MGΔgltA-MV, increased levels of intracellular acetyl-CoA up to sevenfold higher than the wild-type strain. This strain produced 8.0 g/L of mevalonate from 20 g/L of glucose. We also engineered the sugar supply by displaying β-glucosidase (BGL) on the cell surface. When cellobiose was used as carbon source, the strain lacking gnd displaying BGL efficiently consumed cellobiose and produced mevalonate at 5.7 g/L. The yield of mevalonate was 0.25 g/g glucose (1 g of cellobiose corresponds to 1.1 g of glucose). These results demonstrate the feasibility of producing mevalonate from cellobiose or cellooligosaccharides using an engineered E. coli strain.     

Characterization of recombinantE. coli ATCC 11303 (pLOI 297) in the conversion of cellulose and xylose to ethanol

This work describes the characterization of recombinantEsherichia coli ATCC 11303 (pLOI 297) in the production of ethanol from cellulose and xylose. We have examined the fermentation of glucose and xylose, both individually and in mixtures, and the selectivity of ethanol production under various conditions of operation. Xylose metabolism was strongly inhibited by the presence of glucose. Ethanol was a strong inhibitor of both glucose and xylose fermentations; the maximum ethanol levels achieved at 37°C and 42°C were about 50 g/l and 25 g/l respectively. Simmultaneous sacharification and fermentation of cellulose with recombinantE. coli and exogenous cellulose showed a high ethanol yield (84% of theoretical) in the hydrolysis regime of pH 5.0 and 37°C. The selectivity of organic acid formation relative to that of ethanol increased at extreme levels of initial glucose concentration; production of succinic and acetic acids increased at low levels of glucose ( <1 g/l), and lactic acid production increased when initial glucose was higher than 100 g/l.     

Fed-batch culture of Escherichia coli for L-valine production based on in silico flux response analysis

We have previously reported the development of a 100% genetically defined engineered Escherichia coli strain capable of producing L ‐valine from glucose with a high yield of 0.38 g L ‐valine per gram glucose (0.58 mol L ‐valine per mol glucose) by batch culture. Here we report a systems biological strategy of employing flux response analysis in bioprocess development using L ‐valine production by fed‐batch culture as an example. Through the systems‐level analysis, the source of ATP was found to be important for efficient L ‐valine production. There existed a trade‐off between L ‐valine production and biomass formation, which was optimized for the most efficient L ‐valine production. Furthermore, acetic acid feeding strategy was optimized based on flux response analysis. The final fed‐batch cultivation strategy allowed production of 32.3 g/L L ‐valine, the highest concentration reported for E. coli. This approach of employing systems‐level analysis of metabolic fluxes in developing fed‐batch cultivation strategy would also be applicable in developing strategies for the efficient production of other bioproducts. Biotechnol. Bioeng. 2011; 108:934–946. © 2010 Wiley Periodicals, Inc.     

Expression and processing of Vibrio anguillarum zinc-metalloprotease in Escherichia coli

The extracellular zinc-metalloprotease of Vibrio anguillarum is a secreted virulence factor. It is synthesized from the empA gene as a 611-residue preproprotease and processed to the active mature protease (EmpA) with concomitant secretion via the type II secretion pathway. Active EmpA has been found only in the V. anguillarum culture supernatant and the process of the activation seems to vary depending on strains analyzed. To better understand the mechanism of EmpA export and processing, the empA gene was cloned and expressed in Escherichia coli strains. Expression of empA did not have toxic effect on bacterial growth. Rupturing E. coli TOP10 cells by heating in gel-loading buffer resulted in activation of EmpA and severe proteolysis of the samples. In contrast, the same treatment of the E. coli MC4100A strain did not lead to the general proteolysis. In this strain, EmpA was exported into the periplasm via the Sec pathway. The periplasmic EmpA was detected in two active conformations. Therefore, in E. coli processing of EmpA precursor to an active enzyme did not require secretion to the media and the help of other V. anguillarum protein. Like in V. anguillarum, heterologous expression of empA in E. coli showed strain-specific activation process.     

不同浓度外源乙酸钠对耐乙酸大肠埃希菌DA19代谢和关键酶酶活的影响

为研究外源乙酸钠对大肠埃希菌DA19生长代谢的影响,将该菌株在氮源限制基本培养基及添加不同浓度乙酸钠的氮源限制基本培养基中连续培养,测定稳态时生长代谢参数和胞内关键酶酶活。与MN培养基相比,葡萄糖比消耗速率和延胡索酸比生成速率随外源乙酸钠质量浓度增加而逐渐下降,丙酮酸比生成速率则随外源乙酸钠质量浓度增加而明显增加,而乙酸比生成速率则明显降低(除9 g/L乙酸钠外)。磷酸果糖激酶、异柠檬酸脱氢酶、异柠檬酸裂解酶、苹果酸脱氢酶、磷酸烯醇式丙酮酸羧化酶和乙酸激酶酶活随外源乙酸钠质量浓度增加而呈先下降后上升的趋势,而6-磷酸葡萄糖脱氢酶则随着外源乙酸钠质量浓度增加而逐渐降低。为了应对外源乙酸钠压力,大肠埃希菌DA19的生长代谢和中心代谢途径酶活都发生了明显改变。     

Genome-scale metabolic network modeling results in minimal interventions that cooperatively force carbon flux towards malonyl-CoA

Malonyl-coenzyme A is an important precursor metabolite for the biosynthesis of polyketides, flavonoids and biofuels. However, malonyl-CoA naturally synthesized in microorganisms is consumed for the production of fatty acids and phospholipids leaving only a small amount available for the production of other metabolic targets in recombinant biosynthesis. Here we present an integrated computational and experimental approach aimed at improving the intracellular availability of malonyl-CoA in Escherichia coli. We used a customized version of the recently developed OptForce methodology to predict a minimal set of genetic interventions that guarantee a prespecified yield of malonyl-CoA in E. coli strain BL21 Star™. In order to validate the model predictions, we have successfully constructed an E. coli recombinant strain that exhibits a 4-fold increase in the levels of intracellular malonyl-CoA compared to the wild type strain. Furthermore, we demonstrate the potential of this E. coli strain for the production of plant-specific secondary metabolites naringenin (474 mg/L) with the highest yield ever achieved in a lab-scale fermentation process. Combined effect of the genetic interventions was found to be synergistic based on a developed analysis method that correlates genetic modification to cell phenotype, specifically the identified knockout targets (ΔfumC and ΔsucC) and overexpression targets (ACC, PGK, GAPD and PDH) can cooperatively force carbon flux towards malonyl-CoA. The presented strategy can also be readily expanded for the production of other malonyl-CoA-derived compounds like polyketides and biofuels.     

代谢工程改造大肠杆菌合成己二酸

己二酸是一种具有重要应用价值的二元羧酸,是合成尼龙-66的关键前体。目前,生物法生产己二酸存在生产周期长、生产效率低的问题。本研究选择一株野生型高产琥珀酸菌株大肠杆菌(Escherichia coli) FMME N-2为底盘细胞,首先通过引入逆己二酸降解途径的关键酶,成功构建了可合成0.34 g/L己二酸的E. coli JL00菌株;接着,对合成路径限速酶进行表达优化,使E. coli JL01菌株在摇瓶发酵条件下产量达到0.87 g/L;随后,通过敲除sucD基因、过表达acs基因和突变lpd基因的组合策略平衡己二酸合成前体的供应,优化菌株E. coli JL12己二酸产量进一步提升至1.51 g/L;最后,在5 L发酵罐上对己二酸发酵工艺进行优化。工程菌株经72 h分批补料发酵,己二酸的产量达到22.3 g/L,转化率为0.25 g/g,生产强度为0.31 g/(L·h),具备了一定的应用潜力。本研究可为包括己二酸在内的多种二元羧酸细胞工厂的构建提供理论依据和技术基础。     

Caffeic acid production by simultaneous saccharification and fermentation of kraft pulp using recombinant Escherichia coli

Caffeic acid (3,4-dihydroxycinnamic acid) serves as a building block for thermoplastics and a precursor for biologically active compounds and was recently produced from glucose by microbial fermentation. To produce caffeic acid from inedible cellulose, separate hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF) reactions were compared using kraft pulp as lignocellulosic feedstock. Here, a tyrosine-overproducing Escherichia coli strain was metabolically engineered to produce caffeic acid from glucose by introducing the genes encoding a 4-hydroxyphenyllactate 3-hydroxylase (hpaBC) from Pseudomonas aeruginosa and tyrosine ammonia lyase (fevV) from Streptomyces sp. WK-5344. Using the resulting recombinant strain, the maximum yield of caffeic acid in SSF (233 mg/L) far exceeded that by SHF (37.9 mg/L). In the SSF with low cellulase loads (≤2.5 filter paper unit/g glucan), caffeic acid production was markedly increased, while almost no glucose accumulation was detected, indicating that the E. coli cells experienced glucose limitation in this culture condition. Caffeic acid yield was also negatively correlated with the glucose concentration in the fermentation medium. In SHF, the formation of by-product acetate and the accumulation of potential fermentation inhibitors increased significantly with kraft pulp hydrolysate than filter paper hydrolysate. The combination of these inhibitors had synergistic effects on caffeic acid fermentation at low concentrations. With lower loads of cellulase in SSF, less potential fermentation inhibitors (furfural, 5-hydroxymethyfurfural, and 4-hydroxylbenzoic acid) accumulated in the medium. These observations suggest that glucose limitation in SSF is crucial for improving caffeic acid yield, owing to reduced by-product formation and fermentation inhibitor accumulation.

     

Engineering Escherichia coli for efficient production of 5-aminolevulinic acid from glucose

5-Aminolevulinic acid (ALA) recently received much attention due to its potential applications in many fields. In this study, we developed a metabolic strategy to produce ALA directly from glucose in recombinant Escherichia coli via the C5 pathway. The expression of a mutated hemA gene, encoding a glutamyl-tRNA reductase from Salmonella arizona, significantly improved ALA production from 31.1 to 176 mg/L. Glutamate-1-semialdehyde aminotransferase from E. coli was found to have a synergistic effect with HemA^M from S. arizona on ALA production (2052 mg/L). In addition, we identified a threonine/homoserine exporter in E. coli, encoded by rhtA gene, which exported ALA due to its broad substrate specificity. The constructed E. coli DALA produced 4.13 g/L ALA in modified minimal medium from glucose without adding any other co-substrate or inhibitor. This strategy offered an attractive potential to metabolic production of ALA in E. coli.     

Improvement of hEGF production with enhanced cell division ability using dissolved oxygen responses to pulse addition of tryptone

Tryptone has multiple and complex effects on cell physiology and process performance in pulse fed-batch cultivation of recombinant Escherichia coli. By applying feedback control of dissolved oxygen signal responding to pulse in the feed rate, the production of acetate was avoided and the optimization of production of recombinant human epidermal growth factor (hEGF) was successfully achieved. With the addition of an optimum amount of tryptone along with glucose in the pulse fedbatch cultivation of E. coli, the ability of the cell to divide and the stability of the plasmid within the bacteria were improved. Consequently, segregation of the cells into a viable but non-culturable physiological state was alleviated. Addition of tryptone also enhanced cell respiration before and after hEGF expression and thus further benefited the production of recombinant hEGF. Excessive addition of tryptone resulted in low sensitivity of the oscillation of dissolved oxygen signal and poor operability of pulse fed-batch cultivation as this led to an accumulation of acetate, which weakened the dissolved oxygen signal responses. Consequently, the production of recombinant protein was considerably reduced. By combining the process performance and the positive effect of complex media pulse addition on bacterial metabolism, the optimal production conditions of hEGF were successfully determined. A high cell density of 91 g/L dry cell weight was obtained under these optimal production conditions. Furthermore, a high level of 0.24 g/L hEGF was attained leading to a 32.6% increase in product yield as compared to the controls.     

Kultivierung von isogenen E. coli-Stämmen

The strains E. coli C 600 and E. coli C 600 pL CR 665-58 were cultivated on a glucose containing nutrient medium. The cell states of the cell cycle were investigated by means of phased cultivation. The doubling time and the specific carbon-substrate consumption of cells were higher when E. coli C 600 pL CR 665-58 was used. During cell doubling cell states characterized by different specific carbon-substrate consumption coefficients were observed. By adaptation of carbon-substrates supply to the repetitive cell states during continuous cultivation of synchronized bacteria populations the efficiency of cell-mass production was increased by 15 percent.