High level production of supra molecular weight poly (3-hydroxybutyrate) by metabolically engineered<Emphasis Type="Italic">Escherichia coli</Emphasis>

The supra molecular weight poly ([R]-3-hydroxybutyrate) (PHB), having a molecular weight greater than 2 million Da, has recently been found to possess improved mechanical properties compared with the normal molecular weight PHB, which has a molecular weight of less than 1 million Da. However, applications for this PHB have been hampered due to the difficulty of its production. Reported here, is the development of a new metabolically engineeredEscherichia coli strain and its fermentation for high level production of supra molecular weight PHB. RecombinantE. coli strains, harboring plasmids of different copy numbers containing theAlcaligenes latus PHB biosynthesis genes, were cultured and the molecular weights of the accumulated PHB were compared. When the recombinantE. coli XL 1-Blue, harboring a medium-copy-number pJC2 containing theA. latus PHB biosynthesis genes, was cultivated by fed-batch culture at pH 6.0, supra molecular weight PHB could be produced at up to 89.8 g/L with a productivity of 2.07 g PHB/L-h. The molecular weight of PHB obtained under these conditions was as high as 22 MDa, exceeding by an order of magnitude the molecular weight of PHB typically produced inRalstonia eutropha or recombinantE. coli     

Production of Vanillin by Metabolically Engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

E. coli was metabolically engineered to produce vanillin by expression of the fcs and ech genes from Amycolatopsis sp. encoding feruloyl-CoA synthetase and enoyl-CoA hydratase/aldolase, respectively. Vanillin production was optimized by leaky expression of the genes, under the IPTG-inducible trc promoter, in complex 2YT medium. Supplementation with glucose, fructose, galactose, arabinose or glycerol severely decreased vanillin production. The highest vanillin production of 1.1 g l⁻¹ was obtained with cultivation for 48 h in 2YT medium with 0.2% (w/v) ferulate, without IPTG and no supplementation of carbon sources.     

Effect of anaerobic promoters on the microaerobic production of polyhydroxybutyrate (PHB) in recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

Nine anaerobic promoters were cloned and constructed upstream of PHB synthesis genes phbCAB from Ralstonia eutropha for the micro- or anaerobic PHB production in recombinant Escherichia coli. Among the promoters, the one for alcohol dehydrogenase (P _adhE ) was found most effective. Recombinant E. coli JM 109 (pWCY09) harboring P _adhE and phbCAB achieved a 48% PHB accumulation in the cell dry weight after 48 h of static culture compared with only 30% PHB production under its native promoter. Sixty-seven percent PHB was produced in the dry weight (CDW) of an acetate pathway deleted (Δpta deletion) E. coli JW2294 harboring the vector pWCY09. In a batch process conducted in a 5.5-l NBS fermentor containing 3 l glucose LB medium, E. coli JW2294 (pWCY09) grew to 7.8 g/l CDW containing 64% PHB after 24 h of microaerobic incubation. In addition, molecular weight of PHB was observed to be much higher under microaerobic culture conditions. The high activity of P _adhE appeared to be the reason for improved micro- or anaerobic cell growth and PHB production while high molecular weight contributed to the static culture condition.     

Productivity improvement of recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis> fermentation via robust optimization

A nonlinear model of a recombinant Escherichia coli producing porcine growth hormone (pGH) fermentation was developed. The model was used to calculate a glucose feeding and temperature strategy to optimize the production of pGH. Simulations showed that the implementation of optimal feed and temperature profiles was sensitive to the maximum specific growth rate, and a mismatch could result in excessive acetate production and a significant reduction in pGH yield. An optimization algorithm was thus developed, using feedback control, to counter the effects of uncertainty in the specific growth rate and thus determine an optimal operating strategy for pGH production. This policy was experimentally implemented in a 10 L fermenter and resulted in a 125% increase in productivity over the previous best experimental result with this system—in spite of significant plant-model mismatch.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-alanine by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

Escherichia coli W was genetically engineered to produce l-alanine as the primary fermentation product from sugars by replacing the native d-lactate dehydrogenase of E. coli SZ194 with alanine dehydrogenase from Geobacillus stearothermophilus. As a result, the heterologous alanine dehydrogenase gene was integrated under the regulation of the native d-lactate dehydrogenase (ldhA) promoter. This homologous promoter is growth-regulated and provides high levels of expression during anaerobic fermentation. Strain XZ111 accumulated alanine as the primary product during glucose fermentation. The methylglyoxal synthase gene (mgsA) was deleted to eliminate low levels of lactate and improve growth, and the catabolic alanine racemase gene (dadX) was deleted to minimize conversion of l-alanine to d-alanine. In these strains, reduced nicotinamide adenine dinucleotide oxidation during alanine biosynthesis is obligately linked to adenosine triphosphate production and cell growth. This linkage provided a basis for metabolic evolution where selection for improvements in growth coselected for increased glycolytic flux and alanine production. The resulting strain, XZ132, produced 1,279 mmol alanine from 120 g l⁻¹ glucose within 48 h during batch fermentation in the mineral salts medium. The alanine yield was 95% on a weight basis (g g⁻¹ glucose) with a chiral purity greater than 99.5% l-alanine. Electronic supplementary material The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

A recombinant <Emphasis Type="Italic">E. coli</Emphasis> bioprocess for hyaluronan synthesis

An Escherichia coli strain, JM109, was successfully engineered into an efficient hyaluronic acid (HA) producer by co-expressing the only known class-II HA synthase from a Gram-negative bacterium (Pasteurella multocida) and uridine diphosphate-glucose dehydrogenase from E. coli K5 strain. The engineered strain produced about 0.5 g/L HA in shake flask culture and about 2.0–3.8 g/L in a fed-batch fermentation process in a 1-L bioreactor. The sharp increase in viscosity associated with HA accumulation necessitated pure oxygen supplement to maintain fermentation in aerobic regime. Precursor supply during HA synthesis was probed by glucosamine supplement, which shortens biosynthesis pathway and eliminates one step requiring ATP. HA synthesis was increased with glucosamine supplement from 2.7 to 3.7 g/L (37%), which was mirrored with a concomitant 42% decrease in pure oxygen input, suggesting a close connection between energy metabolism and precursor supply. Decoupling HA synthesis from cell growth by using fosfomycin (an inhibitor for cell wall synthesis) led to a 70% increase in HA synthesis, suggesting detrimental effects on HA synthesis from cell growth via precursor competition. This study demonstrates a potentially viable process for HA based on a recombinant E. coli strain. In addition, the precursor supply limitation identified in this study suggests new engineering targets in subsequent metabolic engineering efforts.     

Sucrose and overexpression of trehalose biosynthetic genes (<Emphasis Type="Italic">otsBA</Emphasis>) increase desiccation tolerance of recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

Survival after desiccation was highest for recombinant strains of E. coli engineered to produce ethanol (KO11 and LY163) and lactate (TG106) when sucrose was provided as the fermentable sugar. Desiccation tolerance was lower with glucose and xylose. Further improvements in desiccation tolerance with sucrose were obtained by combining this with increased expression of otsBA genes encoding trehalose biosynthesis, removal of products from metabolism by resuspending in fresh medium, and harvesting cells prior to the end of log phase. With sucrose and otsBA expression, survivals of 20%–80% were readily achieved. Fermentation tests with EM2L, a derivative of LY163 expressing ostBA, demonstrated that ethanol production from seed fermentations begun with desiccated cells is equivalent to that of an undesiccated control.     

Challenges Associated with Heterologous Expression of <Emphasis Type="Italic">Flavobacterium psychrophilum</Emphasis> Proteins in <Emphasis Type="Italic">Escherichia coli</Emphasis>

A two-parameter statistical model was used to predict the solubility of 96 putative virulence-associated proteins of Flavobacterium psychrophilum (CSF259-93) upon over expression in Escherichia coli. This analysis indicated that 88.5% of the F. psychrophilum proteins would be expressed as insoluble aggregates (inclusion bodies). These solubility predictions were verified experimentally by colony filtration blot for six different F. psychrophilum proteins. A comprehensive analysis of codon usage identified over a dozen codons that are used frequently in F. psychrophilum, but that are rarely used in E. coli. Expression of F. psychrophilum proteins in E. coli was often associated with production of minor molecular weight products, presumably because of the codon usage bias between these two organisms. Expression of recombinant protein in the presence of rare tRNA genes resulted in marginal improvements in the expressed products. Consequently, Vibrio parahaemolyticus was developed as an alternative expression host because its codon usage is similar to F. psychrophilum. A full-length recombinant F. psychrophilum hemolysin was successfully expressed and purified from V. parahaemolyticus in soluble form, whereas this protein was insoluble upon expression in E. coli. We show that V. parahaemolyticus can be used as an alternate heterologous expression system that can remedy challenges associated with expression and production of F. psychrophilum recombinant proteins.     

Improving heterologous polyketide production in <Emphasis Type="Italic">Escherichia coli</Emphasis> by overexpression of an <Emphasis Type="Italic">S</Emphasis>-adenosylmethionine synthetase gene

An S-adenosylmethionine synthetase gene (metK) from Streptomyces spectabilis was cloned into an expression plasmid under the control of an inducible T7 promoter and introduced into a strain of Escherichia coli (BAP1(pBP130/pBP144)) capable of producing the polyketide product 6-deoxyerythronolide B (6-dEB). The metK coexpression in BAP1(pBP130/pBP144) improved the specific production of 6-dEB from 10.86 to 20.08 mg l⁻¹ . In an effort to probe the reason for this improvement, a series of gene deletion and expression experiments were conducted based on a metK metabolic pathway that branches between propionyl-CoA (a 6-dEB precursor) and autoinducer compounds. The deletion and expression studies suggested that the autoinducer pathway had a larger impact on improved 6-dEB biosynthesis. Supporting these results were experiments demonstrating the positive effect conditioned media (the suspected location of the autoinducer compounds) had on 6-dEB production. Taken together, the results of this study show an increase in heterologous 6-dEB production concomitant with heterologous metK gene expression and suggest that the mechanism for this improvement is linked to native autoinducer compounds.     

<Emphasis Type="SmallCaps">L</Emphasis>-Tyrosine production by deregulated strains of <Emphasis Type="Italic">Escherichia coli</Emphasis>

The excretion of the aromatic amino acid l-tyrosine was achieved by manipulating three gene targets in the wild-type Escherichia coli K12: The feedback-inhibition-resistant (fbr) derivatives of aroG and tyrA were expressed on a low-copy-number vector, and the TyrR-mediated regulation of the aromatic amino acid biosynthesis was eliminated by deleting the tyrR gene. The generation of this l-tyrosine producer, strain T1, was based only on the deregulation of the aromatic amino acid biosynthesis pathway, but no structural genes in the genome were affected. A second tyrosine over-producing strain, E. coli T2, was generated considering the possible limitation of precursor substrates. To enhance the availability of the two precursor substrates phosphoenolpyruvate and erythrose-4-phosphate, the ppsA and the tktA genes were over-expressed in the strain T1 background, increasing l-tyrosine production by 80% in 50-ml batch cultures. Fed-batch fermentations revealed that l-tyrosine production was tightly correlated with cell growth, exhibiting the maximum productivity at the end of the exponential growth phase. The final l-tyrosine concentrations were 3.8 g/l for E. coli T1 and 9.7 g/l for E. coli T2 with a yield of l-tyrosine per glucose of 0.037 g/g (T1) and 0.102 g/g (T2), respectively.     

Secretory Expression of Nattokinase from <Emphasis Type="Italic">Bacillus subtilis</Emphasis> YF38 in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Nattokinase producing bacterium, B. subtilis YF38, was isolated from douchi, using the fibrin plate method. The gene encoding this enzyme was cloned by polymerase chain reaction (PCR). Cytoplasmic expression of this enzyme in E. coli resulted in inactive inclusion bodies. But with the help of two different signal peptides, the native signal peptide of nattokinase and the signal peptide of PelB, active nattokinase was successfully expressed in E. coli with periplasmic secretion, and the nattokinase in culture medium displayed high fibrinolytic activity. The fibrinolytic activity of the expressed enzyme in the culture was determined to reach 260 urokinase units per micro-liter when the recombinant strain was induced by 0.7 mmol l⁻¹ isopropyl-β-D- thiogalactopyranoside (IPTG) at 20°C for 20 h, resulting 49.3 mg active enzyme per liter culture. The characteristic of this recombinant nattokinase is comparable to the native nattokinase from B. subtilis YF38. Secretory expression of nattokinase in E. coli would facilitate the development of this enzyme into a therapeutic product for the control and prevention of thrombosis diseases.     

Effect of <Emphasis Type="Italic">cra</Emphasis> gene knockout together with <Emphasis Type="Italic">edd</Emphasis> and <Emphasis Type="Italic">iclR</Emphasis> genes knockout on the metabolism in <Emphasis Type="Italic">Escherichia coli</Emphasis>

To elucidate the physiological adaptation of Escherichia coli due to cra gene knockout, a total of 3,911 gene expressions were investigated by DNA microarray for continuous culture. About 50 genes were differentially regulated for the cra mutant. TCA cycle and glyoxylate shunt were down-regulated, while pentose phosphate (PP) pathway and Entner Doudoroff (ED) pathway were up-regulated in the cra mutant. The glucose uptake rate and the acetate production rate were increased with less acetate consumption for the cra mutant. To identify the genes controlled by Cra protein, the Cra recognition weight matrix from foot-printing data was developed and used to scan the whole genome. Several new Cra-binding sites were found, and some of the result was consistent with the DNA microarray data. The ED pathway was active in the cra mutant; we constructed cra.edd double genes knockout mutant to block this pathway, where the acetate overflowed due to the down-regulation of aceA,B and icd gene expressions. Then we further constructed cra.edd.iclR triple genes knockout mutant to direct the carbon flow through the glyoxylate pathway. The cra.edd.iclR mutant showed the least acetate production, resulting in the highest cell yield together with the activation of the glycolysis pathway, but the glucose consumption rate could not be improved. Dayanidhi Sarkar and Khandaker Al Zaid Siddiquee have contributed equally.     

Heterologous expression of the<Emphasis Type="Italic"> Saccharomyces cerevisiae</Emphasis> alcohol acetyltransferase genes in<Emphasis Type="Italic"> Clostridium acetobutylicum</Emphasis> and<Emphasis Type="Italic"> Escherichia coli</Emphasis> for the production of isoamyl acetate

Esters are formed by the condensation of acids with alcohols. The esters isoamyl acetate and butyl butyrate are used for food and beverage flavorings. Alcohol acetyltransferase is one enzyme responsible for the production of esters from acetyl-CoA and different alcohol substrates. The genes ATF1 and ATF2, encoding alcohol acetyltransferases from the yeast Saccharomyces cerevisiae have been sequenced and characterized. The production of acids and alcohols in mass quantities by the industrially important Clostridium acetobutylicum makes it a potential organism for exploitation of alcohol acetyltransferase activity. This report focuses on the heterologous expression of the alcohol acetyltransferases in Escherichia coli and C. acetobutylicum. ATF1 and ATF2 were cloned and expressed in E. coli and ATF2 was expressed in C. acetobutylicum. Isoamyl acetate production from the substrate isoamyl alcohol in E. coli and C. acetobutylicum cultures was determined by head-space gas analysis. Alcohol acetyltransferase I produced more than twice as much isoamyl acetate as alcohol acetyltransferase II when expressed from a high-copy expression vector. The effect of substrate levels on ester production was explored in the two bacterial hosts to demonstrate the efficacy of utilizing ATF1and ATF2 in bacteria for ester production.     

Cloning of <Emphasis Type="Italic">rec</Emphasis>A gene of <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> and phenotypic complementation of <Emphasis Type="Italic">Escherichia coli</Emphasis> recombinant deficient strain

Nucleotide and amino acid sequences of Corynebacterium glutamicum recA genes, from GenBank, were compared in silico. On the basis of the identity found between sequences, two degenerate primers were designed on the two sides of the deduced open reading frame (ORF) of the recA gene. PCR experiments, for amplifying the recA ORF region, were done. pGEM^®-T Easy vector was selected to be used for cloning PCR products. Then recA ORF was placed under the control of Escherichia coli hybrid trc promoter, in pKK388-1 vector. pKK388-1 vector, containing recA ORF, was transformed to E. coli DH5α ΔrecA (recombinant deficient strain), in an attempt to phenotypically complement it. Ultraviolet (u.v.) exposure experiments of the transformed and non-transformed E. coli DH5α ΔrecA cells revealed tolerance of transformed cells up to dose 0.24 J/cm², while non-transformed cells tolerated only up to dose 0.08 J/cm². It is concluded that phenotypic complementation of E. coli DH5α ΔrecA with recA ORF of C. glutamicum, could be achieved and RecA activity could be restored.     

Cloning of a xylanase gene <Emphasis Type="Italic">xyn2A</Emphasis> from rumen fungus <Emphasis Type="Italic">Neocallimastix</Emphasis> sp. GMLF2 in <Emphasis Type="Italic">Escherichia coli</Emphasis> and its partial characterization

Anaerobic fungi belonging to the family Neocallimastigaceae are native inhabitants in the rumen of the most herbivores, such as cattle, sheep and goats. A member of this unique group, Neocallimastix sp. GMLF2 was isolated from cattle feces and screened for its xylanase encoding gene using polymerase chain reaction. The gene coding for a xylanase (xyn2A) was cloned in Escherichia coli and expression was monitored. To determine the enzyme activity, assays were conducted for both fungal xylanase and cloned xylanase (Xyl2A) for supernatant and cell-associated activities. Optimum pH and temperature of the enzyme were found to be 6.5 and 50°C, respectively. The enzyme was stable at 40°C and 50°C for 20 min but lost most of its activity when temperature reached 60°C for 5-min incubation time. Rumen fungal xylanase was mainly released to the supernatant of culture, while cloned xylanase activity was found as cell-associated. Multiple alignment of the amino acid sequences of Xyl2A with published xylanases from various organisms suggested that Xyl2A belongs to glycoside hydrolase family 11.     

Expression of the <Emphasis Type="BoldItalic">Escherichia coli pntAB</Emphasis> genes encoding a membrane-bound transhydrogenase in <Emphasis Type="BoldItalic">Corynebacterium glutamicum</Emphasis> improves <Emphasis Type="SmallCaps">l</Emphasis>-lysine formation

A critical factor in the biotechnological production of l-lysine with Corynebacterium glutamicum is the sufficient supply of NADPH. The membrane-integral nicotinamide nucleotide transhydrogenase PntAB of Escherichia coli can use the electrochemical proton gradient across the cytoplasmic membrane to drive the reduction of NADP⁺ via the oxidation of NADH. As C. glutamicum does not possess such an enzyme, we expressed the E. coli pntAB genes in the genetically defined C. glutamicum lysine-producing strain DM1730, resulting in membrane-associated transhydrogenase activity of 0.7 U/mg protein. When cultivated in minimal medium with 10% (w/v) carbon source, the presence of transhydrogenase slightly reduced glucose consumption, whereas the consumption of fructose, glucose plus fructose, and, in particular, sucrose was stimulated. Biomass was increased by pntAB expression between 10 and 30% on all carbon sources tested. Most importantly, the lysine concentration was increased in the presence of transhydrogenase by ∼10% on glucose, ∼70% on fructose, ∼50% on glucose plus fructose, and even by ∼300% on sucrose. Thus, the presence of a proton-coupled transhydrogenase was shown to be an efficient way to improve lysine production by C. glutamicum. In contrast, pntAB expression had a negative effect on growth and glutamate production of C. glutamicum wild type.