Enhanced production of plasmid DNA by engineered Escherichia coli strains

Escherichia coli strains VH33 (PTS? GalP? strain displaying a strongly reduced overflow metabolism) and VH34 (additionally lacking the pyruvate kinase A) were evaluated for the production of a plasmid DNA (pDNA) vaccine. The parent (W3110) and mutant strains were cultured using 10 g of glucose/L. While the specific growth rates of the three strains were similar, they presented differences in the accumulation of acetate. W3110 accumulated up to 4 g/L of acetate, VH33 produced 1.4 g/L, and VH34 only 0.78 g/L. VH33 and VH34 produced 76% and 300% more pDNA than W3110. Moreover, VH34 demanded 33% less oxygen than VH33 and W3110, which can be advantageous for large-scale applications.     

Microbial production of N-acetylneuraminic acid by genetically engineered Escherichia coli

Previously, we described the production of N-acetylneuraminic acid (NeuAc) from N-acetylglucosamine (GlcNAc) in a system combining recombinant Escherichia coli expressing GlcNAc 2-epimerase (slr1975), E. coli expressing NeuAc synthetase (neuB), and Corynebacterium ammoniagenes. However, this system was unsuitable for large-scale production because of its complexity and low productivity. To overcome these problems, we constructed a recombinant E. coli simultaneously overexpressing slr1975 and neuB. This recombinant E. coli produced 81 mM (25 g/L) NeuAc in 22 h without the addition of C. ammoniagenes cells. For manufacturing on an industrial scale, it is preferable to use unconcentrated culture broth as the source of enzymes, and therefore, a high-density cell culture is required. An acetate-resistant mutant strain of E. coli (HN0074) was selected as the host strain because of its ability to grow to a high cell density. The NeuAc aldolase gene of E. coli HN0074 was disrupted by homologous recombination yielding E. coli N18-14, which cannot degrade NeuAc. After a 22 h reaction with 540 mM (120 g/L) GlcNAc in a 5 L jar fermenter, the culture broth of E. coli N18-14 overexpressing slr1975 and neuB contained 172 mM (53 g/L) NeuAc.     

Rapid and accurate identification of Escherichia coli K-12 strains.

A specific PCR for the identification of K-12 strains, based on the genetic structure of the O-antigen gene cluster (rfb) of Escherichia coli K-12, is described. The assay clearly differentiates E. coli K-12-derived strains from other E. coli strains used in the laboratory or isolated from human and animal clinical specimens, from food, or from environmental samples. Moreover, lineages of K-12 strains can be distinguished with a second PCR based on the same gene cluster. The method presents a useful tool in identifying K-12 for monitoring strains which are used as biologically safe vehicles in biotechnological research, development, and production processes.     

Independent regulation of transport and biosynthesis of arginine in Escherichia coli K-12.

From an arginine auxotrophic strain, a mutant was isolated which is able to utilize d-arginine as a source of l-arginine and shows a high sensitivity to inhibition of growth by canavanine. Transport studies revealed a four- to five-fold increased uptake of arginine and ornithine in cells from the mutant strain. The kinetics of entry of arginine and ornithine evidenced elevated maximal influx values for the arginine- and ornithine-specific transport systems. A close parallel between arginine transport activity and arginine binding activity with one arginine-specific binding periplasmic protein in the mutant strongly suggests that such binding protein is a component of the arginine-specific permease. The affinity between arginine and the binder, isolated from the mutant cells, as well as the electrophoretic mobility of the protein, remain unchanged. The enhanced transport activity of arginine and ornithine with mutant cells is insensitive to repression by arginine or ornithine, whereas the biosynthesis of arginine-forming enzymes is normally repressible. When transport activity was examined in strains with mutations leading to derepression of arginine biosynthesis, the regulation of arginine transport was found to be normal. These studies support the conclusion that arginine transport and arginine biosynthesis, in Escherichia coli K-12, are not regulated in a concerted manner, although both systems may have components in common.     

Polymorphism in the dgt-dapD-tsf region of Escherichia coli K-12 strains.

Restriction analysis of the dapD region cloned from several strains of Escherichia coli, revealed a restriction-fragment length polymorphism (RFLP). This RFLP, which includes the BamHI, EcoRI and SalI sites, may be useful in classification of various E. coli strains.     

Enhanced level and metabolic regulation of methionyl-transfer ribonucleic acid synthetase in different strains of Escherichia coli K-12.

The methionyl-transfer ribonucleic acid (tRNA) synthetase of Escherichia coli K-12 eductants carrying P2-mediated deletions in the region of the structural gene of this enzyme was investigated. No structural alteration of this enzyme was observed in three eductants examined. These were isolated from strain AB311, which had a threefold higher level of methionyl-tRNA synthetase than most haploid strains examined. In two of the three eductants studied, the level of this enzyme was twofold higher than in their parental strain regardless of growth conditions used. In contrast, isoleucyl-, leucyl-, and valyl-tRNA synthetases had similar levels in all strains examined. Like valyl-tRNA synthetase, but to a lesser extent, methionyl-tRNA synthetase was subject to metabolic regulation. Coupling between the level of methionyl-tRNA synthetase and growth rate was observed even in strains that had an enhanced level of methionyl-tRNA synthetase. These results suggest that the formation of methionyl-tRNA synthetase remains subject to metabolic regulation even when the repression-like mechanism that controls the synthesis of this enzyme is altered. In addition, we report that in the merodiploid strain EM20031, which was haploid for the valyl-tRNA synthetase structural gene and diploid for the structural genes of methionyl-tRNA synthetase and D-serine deaminase, the levels of these latter two enzymes varied to a minor yet significant extent with the phosphate concentration of the culture medium; under the same conditions, the level of valyl-tRNA synthetase remained unchanged. Moreover, no variation of the levels of these three enzymes in response to phosphate was observed in the haploid strain HfrH. These results indicate that in the merodiploid strain EM20031, which carries the episome F32, the number of episomes per chromosome varies to some extent according to the phosphate concentration of the culture medium.     

Methanol-based cadaverine production by genetically engineered Bacillus methanolicus strains

Methanol is regarded as an attractive substrate for biotechnological production of value-added bulk products, such as amino acids and polyamines. In the present study, the methylotrophic and thermophilic bacterium Bacillus methanolicus was engineered into a microbial cell factory for the production of the platform chemical 1,5-diaminopentane (cadaverine) from methanol. This was achieved by the heterologous expression of the Escherichia coli genes cadA and ldcC encoding two different lysine decarboxylase enzymes, and by increasing the overall L-lysine production levels in this host. Both CadA and LdcC were functional in B. methanolicus cultivated at 50°C and expression of cadA resulted in cadaverine production levels up to 500 mg l⁻¹ during shake flask conditions. A volume-corrected concentration of 11.3 g l⁻¹ of cadaverine was obtained by high-cell density fed-batch methanol fermentation. Our results demonstrated that efficient conversion of L-lysine into cadaverine presumably has severe effects on feedback regulation of the L-lysine biosynthetic pathway in B. methanolicus. By also investigating the cadaverine tolerance level, B. methanolicus proved to be an exciting alternative host and comparable to the well-known bacterial hosts E. coli and Corynebacterium glutamicum. This study represents the first demonstration of microbial production of cadaverine from methanol.     

Coenzyme Q production by metabolic engineered Escherichia coli strains in defined medium

Bioprocess and Biosystems Engineering - Coenzyme Q (CoQ) plays an important role as an electron transporter in the respiratory chain. It is formed from a benzoquinone ring and an isoprenoid chain...     

Enhanced production of para-hydroxybenzoic acid by genetically engineered Saccharomyces cerevisiae

Saccharomyces cerevisiae is a popular organism for metabolic engineering; however, studies aiming at over-production of bio-replacement precursors for the chemical industry often fail to overcome proof-of-concept stage. When intending to show real industrial attractiveness, the challenge is twofold: formation of the target compound must be increased, while minimizing the formation of side and by-products to maximize titer, rate and yield. To tackle these, the metabolism of the organism, as well as the parameters of the process, need to be optimized. Addressing both we show that S. cerevisiae is well-suited for over-production of aromatic compounds, which are valuable in chemical industry and are particularly useful in space technology. Specifically, a strain engineered to accumulate chorismate was optimized for formation of para-hydroxybenzoic acid. Then a fed-batch bioreactor process was developed, which delivered a final titer of 2.9 g/L, a maximum rate of 18.625 mg_pHBA/(g_CDW × h) and carbon-yields of up to 3.1 mg_pHBA/g_glucose.

     

Homolactate fermentation by metabolically engineered Escherichia coli strains

We report the homofermentative production of lactate in Escherichia coli strains containing mutations in the aceEF, pfl, poxB, and pps genes, which encode the pyruvate dehydrogenase complex, pyruvate formate lyase, pyruvate oxidase, and phosphoenolpyruvate synthase, respectively. The process uses a defined medium and two distinct fermentation phases: aerobic growth to an optical density of about 30, followed by nongrowth, anaerobic production. Strain YYC202 (aceEF pfl poxB pps) generated 90 g/liter lactate in 16 h during the anaerobic phase (with a yield of 0.95 g/g and a productivity of 5.6 g/liter . h). Ca(OH)(2) was found to be superior to NaOH for pH control, and interestingly, significant succinate also accumulated (over 7 g/liter) despite the use of N(2) for maintaining anaerobic conditions. Strain ALS961 (YYC202 ppc) prevented succinate accumulation, but growth was very poor. Strain ALS974 (YYC202 frdABCD) reduced succinate formation by 70% to less than 3 g/liter. (13)C nuclear magnetic resonance analysis using uniformly labeled acetate demonstrated that succinate formation by ALS974 was biochemically derived from acetate in the medium. The absence of uniformly labeled succinate, however, demonstrated that glyoxylate did not reenter the tricarboxylic acid cycle via oxaloacetate. By minimizing the residual acetate at the time that the production phase commenced, the process with ALS974 achieved 138 g/liter lactate (1.55 M, 97% of the carbon products), with a yield of 0.99 g/g and a productivity of 6.3 g/liter . h during the anaerobic phase.     

Suppression by thymidine-requiring mutants of Escherichia coli K-12.

Thymidine-requiring strains of Escherichia coli isolated by trimethoprim selection often simultaneously acquire the ability to suppress bacteriophage T4 nonsense mutations. Suppression is lost in Thy+ revertants and recombinants, but is sometimes retained in thyA plasmid-bearing transformants. Suppression is restricted in Strr derivatives of the Thy- mutants, indicating that suppression occurs at the level of translation.     

Catechol 2,3-oxygenase production by genetically engineered Escherichia coli and its application to catechol determination

Catechol 2,3-oxygenase was produced by Escherichia coli, harbouring the recombinant plasmid pBH100 which contained the pheB gene cloned from phenol-degrading Pseudomonas putida BH, and was applied for the determination of catechol in the liquor. E. coli JM103 (pBH100) and C600 (pBH100) showed, respectively, about 5 and 8.5 times higher activities than that of P. putida BH. Using the crude extract prepared from the culture broth of the recombinant, catechol between 0.1 and 3.0 g/ml could be determined quantitatively in phosphate buffer, synthetic sewage and in mixtures of phenol, benzoate and sallcylate, and also in sodium pyruvate solution. In addition to catechol, 3-methylcatechol, 4-methylcatechol and 4-chlorocatechol could be determined. Oxygenase activity of the crude extract was maintained completely during the 100-day storage at –20°C after being freeze-dried with 10% acelone.M. Fujita, M. Ike, Y. Kawagoshi and N. Shinohara are with the Department of Environmental Engineering, Osaka University, 2-1, Yamadaoka, Suita, Osaka 565, Japan. T. Kamiya is with the Central Research Laboratory of Mitsubishi Electric Co., Amagasaki, Hyogo 661, Japan.     

Orotic acid excretion in some wild-type strains of Escherichia coli K-12.

During rapid growth, the excretion of pyrimidines, predominantly uracil, is a common phenomenon in procaryotes and eucaryotes. In Escherichia coli, some K-12 strains excrete orotic acid and not uracil. This is caused by a mutation in the pyrF gene.     

DNA synthesis in UV-irradiated Escherichia coli K-12 strains carrying dnaA mutations.

Summary In this article we describe some in vivo properties of a coldsensitive ribosomal mutant from Escherichia coli. The mutation affects the rplV gene which is the structural gene of ribosomal protein L22.Our work shows that at 22°C, the biosynthesis of both ribosomal subunits and the maturation processing of 16S and 23S ribosomal RNA are impaired. Integration of our results in a general model of in vivo ribosomal assembly in E. coli is presented.     

L-malate production by metabolically engineered Escherichia coli

Escherichia coli strains (KJ060 and KJ073) that were previously developed for succinate production have now been modified for malate production. Many unexpected changes were observed during this investigation. The initial strategy of deleting fumarase isoenzymes was ineffective, and succinate continued to accumulate. Surprisingly, a mutation in fumarate reductase alone was sufficient to redirect carbon flow into malate even in the presence of fumarase. Further deletions were needed to inactivate malic enzymes (typically gluconeogenic) and prevent conversion to pyruvate. However, deletion of these genes (sfcA and maeB) resulted in the unexpected accumulation of D-lactate despite the prior deletion of mgsA and ldhA and the absence of apparent lactate dehydrogenase activity. Although the metabolic source of this D-lactate was not identified, lactate accumulation was increased by supplementation with pyruvate and decreased by the deletion of either pyruvate kinase gene (pykA or pykF) to reduce the supply of pyruvate. Many of the gene deletions adversely affected growth and cell yield in minimal medium under anaerobic conditions, and volumetric rates of malate production remained low. The final strain (XZ658) produced 163 mM malate, with a yield of 1.0 mol (mol glucose(-1)), half of the theoretical maximum. Using a two-stage process (aerobic cell growth and anaerobic malate production), this engineered strain produced 253 mM malate (34 g liter(-1)) within 72 h, with a higher yield (1.42 mol mol(-1)) and productivity (0.47 g liter(-1) h(-1)). This malate yield and productivity are equal to or better than those of other known biocatalysts.     

Bioaccumulation of mercury from wastewater by genetically engineered Escherichia coli

Genetically engineered E. coli, which express both a Hg2+ transport system and metallothionein, were tested for their ability to remove mercury from wastewater. The wastewater contained more than ten different ions, including 2.58 mg/l mercury, and its pH was 9.6. Mercury uptake was faster from the wastewater than from distilled water, probably because of the higher ionic strength, as the high pH had little effect on mercury accumulation. EDTA also stimulated mercury uptake rather than inhibiting it. A hollow-fiber bioreactor was used to retain induced cells for continuous mercury uptake. The cells removed more than 99% of the mercury in the wastewater and the final amount of mercury accumulated was 26.8 mg/g cell dry weight, while none of the other ions were removed from the water. These results indicated that the induced cells had a high affinity and specificity for mercury.