Production of capsular polysaccharide from Escherichia coli K4 for biotechnological applications

The production of industrially relevant microbial polysaccharides has recently gained much interest. The capsular polysaccharide of Escherichia coli K4 is almost identical to chondroitin, a commercially valuable biopolymer that is so far obtained from animal tissues entailing complex and expensive extraction procedures. In the present study, the production of capsular polysaccharide by E. coli K4 was investigated taking into consideration a potential industrial application. Strain physiology was first characterized in shake flask experiments to determine the optimal culture conditions for the growth of the microorganism and correlate it to polysaccharide production. Results show that the concentration of carbon source greatly affects polysaccharide production, while the complex nitrogen source is mainly responsible for the build up of biomass. Small-scale batch processes were performed to further evaluate the effect of the initial carbon source concentration and of growth temperatures on polysaccharide production, finally leading to the establishment of the medium to use in following fermentation experiments on a bigger scale. The fed-batch strategy next developed on a 2-L reactor resulted in a maximum cell density of 56 g_cww/L and a titre of capsular polysaccharide equal to 1.4 g/L, approximately ten- and fivefold higher than results obtained in shake flask and 2-L batch experiments, respectively. The release kinetics of K4 polysaccharide into the medium were also explored to gain insight into the mechanisms underlying a complex aspect of the strain physiology.     

KfoE encodes a fructosyltransferase involved in capsular polysaccharide biosynthesis in Escherichia coli K4

Escherichia coli K4 synthesizes a capsular polysaccharide (CPS) consisting of a fructose-branched chondroitin (GalNAc-GlcA(fructose)n), which is a biosynthetic precursor of chondroitin sulfate. Here, the role of kfoE in the modification of the chondroitin backbone was investigated using knock-out and recombinant complementation experiments. kfoE disruption and complementation had no significant effect on cell growth. CPS production was increased by 15 % in the knock-out strain, and decreased by 21 % in the knock-out strain complemented with recombinant kfoE. CPS extracted from the knock-out strain was chondroitin, whereas CPS extracted from the complemented strain was a fructose-branched chondroitin. The results demonstrated that the kfoE gene product altered the fructose group at the C3 position of the GlcA residue during production of K4CPS.     

Production of flavonoids and polysaccharide by adding elicitor in different cellular cultivation processes of Glycyrrhiza uralensis Fisch

In this study, callus and cell suspension were induced from seedlings of licorice (G. uralensis). In addition, it was revealed that the appropriate concentration of sucrose could promote the callus growth and increase the content of polysaccharide. The methyl jasmonate (MJ) and phenylalanine (PHE) could enhance the callus growth and content of flavonoids for G. uralensis. For producing more flavonoids and polysaccharide, two-stage cultivation was performed. In the first step, 30 g L^?1 sucrose was fed into a 5-L balloon-type bubble bioreactor on 8th day of culture to enhance cell production and metabolite production. In a two-stage cultivation process, PHE (2 mM) and MJ (5 mg L^?1) were added into a 5-L balloon-type bubble bioreactor after 10 days of culture. Using a fed-batch cultivation strategy (30 g L^?1 sucrose was fed into a 5-L balloon-type bubble bioreactor on 8th day), polysaccharide production was enhanced to 1.19 g L^?1, which was 2.12-fold greater than that in batch cultivation. The flavonoids yield (55.42 mg L^?1) which was about 22 % higher than that in batch cultivation was obtained on 21st day. In a two-stage cultivation process, the polysaccharide content was increased by 1.14- and 2.12-fold compared with fed-batch cultivation and batch cultivation on 15th day. Meanwhile, total flavonoids yield (132.36 mg L^?1) on 15th day, was increased by 2.26- and 2.67-fold compared with fed-batch cultivation and batch cultivation. In conclusion, two-stage cultivation process combined with the sucrose and elicitor treatment could promote both the callus growth and the secondary metabolites accumulation.     

High cell density cultivation of <Emphasis Type="Italic">Escherichia coli</Emphasis> K4 in a microfiltration bioreactor: a step towards improvement of chondroitin precursor production

Background  

The bacteria Escherichia coli K4 produces a capsular polysaccharide (K4 CPS) whose backbone is similar to the non sulphated chondroitin chain. The chondroitin sulphate is one of the major components of the extra-cellular matrix of the vertebrate connective tissues and a high value molecule, widely employed as active principle in the treatment of osteoarthritis. It is usually obtained by extraction from animal tissues, but the risk of virus contaminations, as well as the scarceness of raw material, makes this productive process unsafe and unable to satisfy the growing market demand. In previous studies a new biotechnological process to produce chondroitin from Escherichia coli K4 capsular polysaccharide was investigated and a 1.4 g·L^-1 K4 CPS concentration was reached using fed-batch fermentation techniques. In this work, on the trail of these results, we exploited new fermentation strategies to further improve the capsular polysaccharide production.     

Sequence analysis and distribution of an IS3-like insertion element isolated from Salmonella enteritidis

The nucleotide sequence of a 3 kb region immediately upstream of the sef operon of Salmonella enteritidis was determined. A 1230 base pair insertion sequence which shared sequence identity (>75%) with members of the IS3 family was revealed. This element, designated IS1230, had almost identical (90% identity) terminal inverted repeats to Escherichia coli IS3 but unlike other IS3-like sequences lacked the two characteristic open reading frames which encode the putative transposase. S. enteritidis possessed only one copy of this insertion sequence although Southern hybridisation analysis of restriction digests of genomic DNA revealed another fragment located in a region different from the sef operon which hybridised weakly which suggested the presence of an IS1230 homologue. The distribution of IS1230 and IS1230-like elements was shown to be widespread amongst salmonellas and the patterns of restriction fragments which hybridised differed significantly between Salmonella serotypes and it is suggested that IS1230 has potential for development as a differential diagnostic tool.     

Chaperone-assisted expression of KfiC glucuronyltransferase from <Emphasis Type="Italic">Escherichia coli</Emphasis> K5 leads to heparosan production in <Emphasis Type="Italic">Escherichia coli</Emphasis> BL21 in absence of the stabilisator KfiB

The heparosan synthase of Escherichia coli K5 is composed of the glycosyltransferases KfiA and KfiC which synthesize the polysaccharide heparosan (N-acetylheparosan). A third protein, KfiB, is required to stabilize the KfiAC complex in the bacteria and to transport this complex to the inner membrane where the initiation of polymerization occurs. In this report, we fused KfiC with the E. coli trigger factor (TF) to stabilize KfiC, thus activating the enzyme in the absence of KfiB. Different recombinant plasmids were constructed to compare the impact of the presence or absence of KfiB and the presence of the trigger factor as a fusion protein. Several E. coli BL21-derived strains were transformed with recombinant plasmids and cultivated in fed-batch conditions on minimal medium. The bTCA strain overexpressing fused TF-KfiC together with KfiA and KfiD, but lacking KfiB produced 1.5 g/L of total heparosan after 24 h of fed-batch cultivation. This heparosan was essentially intracellular early in the culture, providing evidence that KfiB primarily plays a role in the exportation process. However, over time, heparosan became mostly extracellular, likely due to passive diffusion or partial cell disruption upon product accumulation.     

Prokaryotic Expression and Purification of Soluble Maize Ac Transposase

Transposons are mobile genetic elements that are found in all eukaryotic and prokaryotic species studied to date. The Maize Activator (Ac) transposase recognizes and excises Ac and Dissociation (Ds) elements and mediates insertion elsewhere in the genome. Insertions of Ds can cause disruption in gene sequences and hence are important functional genomics tool for tagging and cloning of unknown gene sequences. The involvement of Ac transposase (AcTPase) in Ds movement is well documented; however, protein structure and function of AcTPase is poorly understood. To express the maize AcTPase in E. coli, Ac cDNA was synthesized with an N-terminal 6xHis tag and cloned in pTrcAc expression vector. The expression cassette was induced in Rosetta2 (DE3) E. coli lines. End-point RT-PCR confirmed the integrity of AcTPase mRNA during cell culture. Autoinducing cultures grown at 37 °C produced prominent partial AcTPase products of ~40 kDa and ~70 kDa. Trypsin digestion and mass spectrometry analyses confirmed AcTPase in both the eluted peptides. When the cultures were grown at 22–25 °C for 24 h the expected ~90 kDa AcTPase soluble product was detected. The successful expression of full length AcTPase in soluble form allows further investigation of its structure and function.     

Functional activity of transposase of Bordetella pertussis IS element in Escherichia coli cells

An Escherichia coli strain producing transposase of a repeated sequence of Bordetella pertussis chromosome (RSBP) was constructed. A defective MGE-helper plasmid method, which allowed the determination of transposase functional activity was developed. It was shown that transposase synthesized in E. coli cells ensures transposition of “defective” RSBP into the host chromosome. Overexpression of transposase was shown to markedly decrease the vital activity of E. coli cells under selective cultivation conditions. Reasons for a decrease in viability transposase-producing cells are discussed. Results showing the impact of transposase on replication of recombinant plasmids and E. coli cell division were obtained.     

An insertion sequence unique to Frankia strain ArI5

At the genetic level, understanding of symbiotic nitrogen fixation by Frankia is limited to nif functions that are highly conserved among all organisms. The genetics and biochemistry of nodulation are largely unexplored because of a complete lack of genetic tools. In other bacteria, mobile genetic elements such as insertion sequences (IS) and transposons are commonly used to create mutations and insert new genetic material. We have characterized a 4 kbp segment of DNA from Frankia strain ArI5 that has the hallmarks of a mobile genetic element, inverted repeats flanking a gene encoding a transposase. There are at least six copies of this element in strain ArI5 but none in either strain CcI3 or CpI1. The inverted repeats are 17 nt long and separated by 2156 bp. Within that region are two, overlapping ORFs that each encode a transposase. RT-PCR analysis of RNA from Frankia ArI5 cells conclusively demonstrates the expression of one transposase gene and suggests that both may be transcribed. Numerous attempts to clone the intact IS in E. coli were unsuccessful suggesting that the element may be unstable in this context. A clone containing the complete IS was constructed in E. coli then modified by insertion of the kanamycin (KAN) resistance gene from Tn5. A fragment of DNA including the inverted repeats, transposase genes and KAN gene, was transferred to the suicide vector pJBSD1. The construct, pFRISK, was transformed into E. coli to search for transposition events.     

Transposases are responsible for the target specificity of IS1397 and ISKpn1 for two different types of palindromic units (PUs)

Insertion sequences (IS)1397 and ISKpn1, found in Escherichia coli and Klebsiella pneumoniae, respectively, are IS3 family members that insert specifically into short palindromic repeated sequences (palindromic units or PUs). In this paper, we first show that although PUs are naturally absent from extrachromosomal elements, both ISs are able to transpose from the chromosome or from a plasmid into PUs artificially introduced into target plasmids. We also show that ISKpn1 target specificity is restricted to K.pneumoniae Z¹ PU type, whereas IS1397 target specificity is less stringent since the IS targets the three E.coli Y, Z¹ and Z² PU types indifferently. Experiments of transposition of both ISs driven by both transposases demonstrate that the inverted repeats flanking the ISs are not responsible for this target specificity, which is entirely due to the transposase itself. Implications on ISs evolution are presented.     

Fermentation characterization of an L-tryptophan producing Escherichia coli strain with inactivated phosphotransacetylase

Acetate is a primary inhibitory metabolite in Escherichia coli cultivation which is detrimental to bacterial growth and the formation of desired products. It can be derived from acetyl coenzyme A by the phosphotransacetylase (Pta)–acetate kinase (AckA) pathway. In this study, the fermentation characteristics of Pta mutant strain E. coli TRTHΔpta were compared with those of the control strain E. coli TRTH in a 30-L fermentor. The effects of glucose concentration and dissolved oxygen (DO) level were investigated, and the results suggest that DO and glucose concentration are vital influencing parameters for the production of L-tryptophan. Based on our experimental results, we then tested a DO-stat fed-batch fermentation strategy. When DO was controlled at about 20 % during L-tryptophan fermentation in the DO-stat fed-batch system, the pta mutant was able to maintain a higher growth rate at the exponential phase, and the final biomass and L-tryptophan production were increased to 55.3 g/L and 35.2 g/L, respectively. Concomitantly, as the concentration of acetate decreased to 0.7 g/L, the accumulation of pyruvate and lactate increased in the mutant strain as compared with the control strain. This characterization of the recombinant mutant strain provides useful information for the rational modification of metabolic fluxes to improve tryptophan production.     

In silico aided metabolic engineering of Klebsiella oxytoca and fermentation optimization for enhanced 2,3-butanediol production

Klebsiella oxytoca naturally produces a large amount of 2,3-butanediol (2,3-BD), a promising bulk chemical with wide industrial applications, along with various byproducts. In this study, the in silico gene knockout simulation of K. oxytoca was carried out for 2,3-BD overproduction by inhibiting the formation of byproducts. The knockouts of ldhA and pflB genes were targeted with the criteria of maximization of 2,3-BD production and minimization of byproducts formation. The constructed K. oxytoca ΔldhA ΔpflB strain showed higher 2,3-BD yields and higher final concentrations than those obtained from the wild-type and ΔldhA strains. However, the simultaneous deletion of both genes caused about a 50 % reduction in 2,3-BD productivity compared with K. oxytoca ΔldhA strain. Based on previous studies and in silico investigation that the agitation speed during 2,3-BD fermentation strongly affected cell growth and 2,3-BD synthesis, the effect of agitation speed on 2,3-BD production was investigated from 150 to 450 rpm in 5-L bioreactors containing 3-L culture media. The highest 2,3-BD productivity (2.7 g/L/h) was obtained at 450 rpm in batch fermentation. Considering the inhibition of acetoin for 2,3-BD production, fed-batch fermentations were performed using K. oxytoca ΔldhA ΔpflB strain to enhance 2,3-BD production. Altering the agitation speed from 450 to 350 rpm at nearly 10 g/L of acetoin during the fed-batch fermentation allowed for the production of 113 g/L 2,3-BD, with a yield of 0.45 g/g, and for the production of 2.1 g/L/h of 2,3-BD.     

Improved extracellular expression and high-cell-density fed-batch fermentation of chitosanase from <Emphasis Type="Italic">Aspergillus Fumigatus</Emphasis> in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Chitosanase (CSN) from Aspergillus fumigatus has good thermal stability, wide pH range duration, and effective hydrolysis for chitosan. Inhere, CSN was successfully expressed in Escherichia coli followed by extracellular secretion under the guidance of an N-terminal signal peptide PelB, which effectively prompted its secretion out of E. coli cells. To facilitate its later purification, N-terminal or C-terminal 6xHis epitope tag was added to the PelB-CSN protein complex. Our results indicated that PelB-CSN without 6xHis-tag (PelB-CSN) or with N-terminal 6xHis-tag (PelB-CSN-N) can both be effectively secreted into the medium, while CSN with 6xHis-tag anchored at C-terminus was expressed as inclusion bodies. Process optimization strategies were further developed to improve the secretion efficiency of recombinant PelB-CSN-N in E. coli. Under the induction of 10 g/L lactose in shake-flask culture, the extracellular activity of CSN reached 6015 U/mL at 25 °C in TB medium containing 1 % glycine. Moreover, a fed-batch fermentation strategy for high-cell-density cultivation was applied in a 5-L fermenter, increasing the extracellular CSN activity to 14,000 U/mL in 2-day fermentation with the optimal addition of lactose and glycine.     

Effects of NADH kinase on NADPH-dependent biotransformation processes in Escherichia coli

Sufficient supply of NADPH is one of the most important factors affecting the productivity of biotransformation processes. In this study, construction of an efficient NADPH-regenerating system was attempted using direct phosphorylation of NADH by NADH kinase (Pos5p) from Saccharomyces cerevisiae for producing guanosine diphosphate (GDP)-l-fucose and ε-caprolactone in recombinant Escherichia coli. Expression of Pos5p in a fed-batch culture of recombinant E. coli producing GDP-l-fucose resulted in a maximum GDP-l-fucose concentration of 291.5 mg/l, which corresponded to a 51 % enhancement compared with the control strain. In a fed-batch Baeyer–Villiger (BV) oxidation of cyclohexanone using recombinant E. coli expressing Pos5p, a maximum ε-caprolactone concentration of 21.6 g/l was obtained, which corresponded to a 96 % enhancement compared with the control strain. Such an increase might be due to the enhanced availability of NADPH in recombinant E. coli expressing Pos5p. These results suggested that efficient regeneration of NADPH was possible by functional expression of Pos5p in recombinant E. coli, which can be applied to other NADPH-dependent biotransformation processes in E. coli.     

Production of recombinant Chikungunya virus envelope 2 protein in Escherichia coli

Chikungunya, a mosquito-borne viral disease caused by Chikungunya virus (CHIKV), has drawn substantial attention after its reemergence causing massive outbreaks in tropical regions of Asia and Africa. The recombinant envelope 2 (rE2) protein of CHIKV is a potential diagnostic as well as vaccine candidate. Development of cost-effective cultivation media and appropriate culture conditions are generally favorable for large-scale production of recombinant proteins in Escherichia coli. The effects of medium composition and cultivation conditions on the production of recombinant Chikungunya virus E2 (rCHIKV E2) protein were investigated in shake flask culture as well as batch cultivation of Escherichia coli. Further, the fed-batch process was also carried out for high cell density cultivation of E. coli expressing rE2 protein. Expression of rCHIKV E2 protein in E. coli was induced with 1 mM isopropyl-beta-thiogalactoside (IPTG) at ~23 g dry cell weight (DCW) per liter of culture and yielded an insoluble protein aggregating to form inclusion bodies. The final DCW after fed-batch cultivation was ~35 g/l. The inclusion bodies were isolated, solubilized in 8 M urea and purified through affinity chromatography to give a final product yield of ~190 mg/l. The reactivity of purified E2 protein was confirmed by Western blotting and enzyme-linked immunosorbent assay. These results show that rE2 protein of CHIKV may be used as a diagnostic reagent or for further prophylactic studies. This approach of producing rE2 protein in E. coli with high yield may also offer a promising method for production of other viral recombinant proteins.     

Monosaccharide precursors for boosting chondroitin-like capsular polysaccharide production

Chondroitin sulfate is a well-known bioactive molecule, widely used as an anti-osteoarthritis drug, that is nowadays mainly produced by animal tissue sources with unsafe extraction procedures. Recent studies have explored an integrated biotechnological–chemical strategy to obtain a chondroitin sulfate precursor from Escherichia coli K4 capsular polysaccharide, demonstrating the influence of environmental and growth conditions on capsule synthesis. In this research work, the flexibility of the strain biosynthetic machinery was investigated to enhance the K4 capsular polysaccharide production by supplementing the growth medium with the monosaccharides (glucuronic acid, galactosamine and fructose) that constitute the chain. Shake flask experiments were performed by adding the sugars singularly or together, by testing monosaccharide different concentrations and times of addition and by observing the bacterial sugar consumption. A K4 capsular polysaccharide production enhancement, compared to the control, was observed in all cases of supplementation and, in particular, significant 68 and 57 % increases were observed when adding 0.385 mM glucuronic acid plus galactosamine or 0.385 mM fructose, respectively. Increased expression levels of the gene kfoC, coding for a K4 polymerase, evaluated in different growth conditions, confirmed the results at the molecular level. Furthermore, batch fermentations, performed in lab-scale reactors (2 L), allowed to double the K4 capsular polysaccharide production values obtained in shake flask conditions, by means of a strict control of the growth parameters.     

Stem Loop Sequences Specific to Transposable Element IS605 Are Found Linked to Lipoprotein Genes in Borrelia Plasmids

Background

Plasmids of Borrelia species are dynamic structures that contain a large number of repetitive genes, gene fragments, and gene fusions. In addition, the transposable element IS605/200 family, as well as degenerate forms of this IS element, are prevalent. In Helicobacter pylori, flanking regions of the IS605 transposase gene contain sequences that fold into identical small stem loops. These function in transposition at the single-stranded DNA level.

Methodology/Principal Findings

In work reported here, bioinformatics techniques were used to scan Borrelia plasmid genomes for IS605 transposable element specific stem loop sequences. Two variant stem loop motifs are found in the left and right flanking regions of the transposase gene. Both motifs appear to have dispersed in plasmid genomes and are found “free-standing” and phylogenetically conserved without the associated IS605 transposase gene or the adjacent flanking sequence. Importantly, IS605 specific stem loop sequences are also found at the 3′ ends of lipoprotein genes (PFam12 and PFam60), however the left and right sequences appear to develop their own evolutionary patterns. The lipoprotein gene-linked left stem loop sequences maintain the IS605 stem loop motif in orthologs but only at the RNA level. These show mutations whereby variants fold into phylogenetically conserved RNA-type stem loops that contain the wobble non-Watson-Crick G-U base-pairing. The right flanking sequence is associated with the family lipoprotein-1 genes. A comparison of homologs shows that the IS605 stem loop motif rapidly dissipates, but a more elaborate secondary structure appears to develop in its place.

Conclusions/Significance

Stem loop sequences specific to the transposable element IS605 are present in plasmid regions devoid of a transposase gene and significantly, are found linked to lipoprotein genes in Borrelia plasmids. These sequences are evolutionarily conserved and/or structurally developed in an RNA format. The findings show that IS605 stem loop sequences are multifaceted and are selectively conserved during evolution when the transposable element dissipates.     

Production of 3-hydroxypropionic acid from glycerol by acid tolerant Escherichia coli

The biological production of 3-hydroxypropionic acid (3-HP) has attracted significant attention because of its industrial importance. The low titer, yield and productivity, all of which are related directly or indirectly to the toxicity of 3-HP, have limited the commercial production of 3-HP. The aim of this study was to identify and select a 3-HP tolerant Escherichia coli strain among nine strains reported to produce various organic acids efficiently at high titer. When transformed with heterologous glycerol dehydratase, reactivase and aldehyde dehydrogenase, all nine E. coli strains produced 3-HP from glycerol but the level of 3-HP production, protein expression and activities of the important enzymes differed significantly according to the strain. Two E. coli strains, W3110 and W, showed higher levels of growth than the others in the presence of 25 g/L 3-HP. In the glycerol fed-batch bioreactor experiments, the recombinant E. coli W produced a high level of 3-HP at 460 ± 10 mM (41.5 ± 1.1 g/L) in 48 h with a yield of 31 % and a productivity of 0.86 ± 0.05 g/L h. In contrast, the recombinant E. coli W3110 produced only 180 ± 8.5 mM 3-HP (15.3 ± 0.8 g/L) in 48 h with a yield and productivity of 26 % and 0.36 ± 0.02 g/L h, respectively. This shows that the tolerance to and the production of 3-HP differ significantly among the well-known, similar strains of E. coli. The titer and productivity obtained with E. coli W were the highest reported thus far for the biological production of 3-HP from glycerol by E. coli.     

Mechanisms of increasing expression of a yeast gene in Escherichia coli

Escherichia coli strains with increased expression of the cloned yeast his3 gene were selected. In some mutants an E. coli chromosomal locus is altered; in others the yeast his3 sequence is affected. Alterations of the his3 sequence include a point mutation, deletion, and IS2 insertion. When IS2 inserts into the yeast sequence, all pre-existing copies of IS2 are maintained in their original location in the E. coli chromosome. The results indicate that E. coli can employ a variety of mechanisms to increase expression of a foreign gene.     

Enhanced virulence effect of K1 polysaccharide in neonatal rats challenged withE. coli

Purified K1 polysaccharide enhanced the virulence of non-K1Escherichia coli species when given by orogastric feeding to neonatal rats. Neonatal rats developedE. coli bacteremia when K1 polysaccharide was given concomitantly with non-K1E. coli, whereasE. coli bacteremia did not develop when non-K1E. coli was given alone.E. coli K1 species did cause bacteremia and meningitis when fed to neonatal rats. The mechanism by which k1 polysaccharide enhances virulence can be studied with this model of bacteremia development in neonatal rats.