Metabolic engineering of Escherichia coli BL21 for biosynthesis of heparosan, a bioengineered heparin precursor

As a precursor of bioengineered heparin, heparosan is currently produced from Escherichia coli K5, which is pathogenic bacteria potentially causing urinary tract infection. Thus, it would be advantageous to develop an alternative source of heparosan from a non-pathogeneic strain. In this work we reported the biosynthesis of heparosan via the metabolic engineering of non-pathogenic E. coli BL21 as a production host. Four genes, KfiA, KfiB, KfiC and KfiD, encoding enzymes for the biosynthesis of heparosan in E. coli K5, were cloned into inducible plasmids pETDuet-1 and pRSFDuet-1 and further transformed into E. coli BL21, yielding six recombinant strains as follows: sA, sC, sAC, sABC, sACD and sABCD. The single expression of KfiA (sA) or KfiC (sC) in E. coli BL21 did not produce heparosan, while the co-expression of KfiA and KfiC (sAC) could produce 63mg/L heparosan in shake flask. The strain sABC and sACD could produce 100 and 120mg/L heparosan, respectively, indicating that the expression of KfiB or KfiD was beneficial for heparosan production. The strain sABCD could produce 334mg/L heparosan in shake flask and 652mg/L heparosan in 3-L batch bioreactor. The heparosan yield was further increased to 1.88g/L in a dissolved oxygen-stat fed-batch culture in 3-L bioreactor. As revealed by the nuclear magnetic resonance analysis, the chemical structure of heparosan from recombinant E. coli BL21 and E. coli K5 was identical. The weight average molecular weight of heparosan from E. coli K5, sAC, sABC, sACD, and sABCD was 51.67, 39.63, 91.47, 64.51, and 118.30kDa, respectively. This work provides a viable process for the production of heparosan as a precursor of bioengineered heparin from a safer bacteria strain.     

Quantitation of heparosan with heparin lyase III and spectrophotometry

Heparosan is Escherichia coli K5 capsule polysaccharide, which is the key precursor for preparing bioengineered heparin. A rapid and effective quantitative method for detecting heparosan is important in the large-scale production of heparosan. Heparin lyase III (Hep III) effectively catalyzes the heparosan depolymerization, forming unsaturated disaccharides that are measurable using a spectrophotometer at 232 nm. We report a new method for the quantitative detection of heparosan with heparin lyase III and spectrophotometry that is safer and more specific than the traditional carbazole assay. In an optimized detection system, heparosan at a minimum concentration of 0.60 g/L in fermentation broth can be detected.     

Effects of carbon sources and feeding strategies on heparosan production by Escherichia coli K5

This work aimed to develop an optimal carbon source feeding strategy to achieve maximal production of heparosan as a precursor of bioengineered heparin by Escherichia coli K5. Glycerol gave higher heparosan titer and productivity compared to glucose. The maximum heparosan production (187 mg/L) and heparosan productivity (5.19 mg/L/h) in glycerol-defined medium were 26.4% higher than the heparosan production (148 mg/L) and heparosan productivity (4.11 mg/L/h) in glucose-defined medium. DO-stat feeding approach as compared to pH-stat feeding, exponential feeding, exponential combined with pH-stat feeding, and constant rate feeding gave the highest heparosan titer at 8.63 g/L, which was nine times that of batch culture. The obtained optimal glycerol feeding strategy may be useful for the scaling-up of microbial heparosan production.     

Controlled Photochemical Depolymerization of K5 Heparosan, a Bioengineered Heparin Precursor

Heparosan is a polysaccharide, which serves as the critical precursor in heparin biosynthesis and chemoenzymatic synthesis of bioengineered heparin. Because the molecular weight of microbial heparosan is considerably larger than heparin, the controlled depolymerization of microbial heparosan is necessary prior to its conversion to bioengineered heparin. We have previously reported that other acidic polysaccharides could be partially depolymerized with maintenance of their internal structure using a titanium dioxide-catalyzed photochemical reaction. This photolytic process is characterized by the generation of reactive oxygen species that oxidize individual saccharide residues within the polysaccharide chain. Using a similar approach, a microbial heparosan from Escherichia coli K5 of molecular weight >15,000 was depolymerized to a heparosan of molecular weight 8,000. The (1)H-NMR spectra obtained showed that the photolyzed heparosan maintained the same structure as the starting heparosan. The polysaccharide chains of the photochemically depolymerized heparosan were also characterized by electrospray ionization-Fourier-transform mass spectrometry. While the chain of K5 heparosan starting material contained primarily an even number of saccharide residues, as a result of coliphage K5 lyase processing, both odd and even chain numbers were detected in the photochemically-depolymerized heparosan. These results suggest that the photochemical depolymerization of heparosan was a random process that can take place at either the glucuronic acid or the N-acetylglucosamine residue within the heparosan polysaccharide.     

Control of the heparosan <Emphasis Type="Italic">N</Emphasis>-deacetylation leads to an improved bioengineered heparin

The production of the anticoagulant drug heparin from non-animal sources has a number of advantages over the current commercial production of heparin. These advantages include better source material availability, improved quality control, and reduced concerns about animal virus or prion impurities. A bioengineered heparin would have to be chemically and biologically equivalent to be substituted for animal-sourced heparin as a pharmaceutical. In an effort to produce bioengineered heparin that more closely resembles pharmaceutical heparin, we have investigated a key step in the process involving the N-deacetylation of heparosan. The extent of N-deacetylation directly affects the N-acetyl/N-sulfo ratio in bioengineered heparin and also impacts its molecular weight. Previous studies have demonstrated that the presence and quantity of N-acetylglucosamine in the nascent glycosaminoglycan chain, serving as the substrate for the subsequent enzymatic modifications (C5 epimerization and O-sulfonation), can impact the action of these enzymes and, thus, the content and distribution of iduronic acid and O-sulfo groups. In this study, we control the N-deacetylation of heparosan to produce a bioengineered heparin with an N-acetyl/N-sulfo ratio and molecular weight that is similar to animal-sourced pharmaceutical heparin. The structural composition and anticoagulant activity of the resultant bioengineered heparin was extensively characterized and compared to pharmaceutical heparin obtained from porcine intestinal mucosa.     

E. coli K5 fermentation and the preparation of heparosan,a bioengineered heparin precursor

Heparosan is an acidic polysaccharide natural product, which serves as the critical precursor in heparin biosynthesis and in the chemoenzymatic synthesis of bioengineered heparin. Heparosan is also the capsular polysaccharide of Escherichia coli K5 strain. The current study was focused on the examination of the fermentation of E. coli K5 with the goal of producing heparosan in high yield and volumetric productivity. The structure and molecular weight properties of this bacterial heparosan were determined using polyacrylamide gel electrophoresis (PAGE) and Fourier transform mass spectrometry. Fermentation of E. coli K5 in a defined medium using exponential fed‐batch glucose addition with oxygen enrichment afforded heparosan at 15 g/L having a number average molecular weight of 58,000 Da and a weight average molecular weight of 84,000 Da. Biotechnol. Bioeng. 2010;107: 964–973. © 2010 Wiley Periodicals, Inc.     

High cell density cultivation of a recombinant E. coli strain expressing a key enzyme in bioengineered heparin production

A bioengineered heparin, as a replacement for animal-derived heparin, is under development that relies on the fermentative production of heparosan by Escherichia coli K5 and its subsequent chemoenzymatic modification using biosynthetic enzymes. A critical enzyme in this pathway is the mammalian 6-O-sulfotransferase (6-OST-1) which specifically sulfonates the glucosamine residue in a heparin precursor. This mammalian enzyme, previously cloned and expressed in E. coli, is required in kilogram amounts if an industrial process for bioengineered heparin is to be established. In this study, high cell density cultivation techniques were exploited to obtain recombinant 6-OST-1. Physiological studies were performed in shake flasks to establish optimized growth and production conditions. Induction strategies were tested in fed-batch experiments to improve yield and productivity. High cell density cultivation in 7-l culture, together with a coupled inducer strategy using isopropyl β-d-1-thiogalactopyranoside and galactose, afforded 482 mg?l^?1 of enzyme with a biomass yield of 16.2 mg?g_cdw ^?1 and a productivity of 10.5 mg?l^?1?h^?1.     

Response surface optimization of the heparosan N-deacetylation in producing bioengineered heparin

The chemical step in the chemoenzymatic synthesis of bioengineered heparin has been examined and optimized statistically using a response surface methodology. A four factor, two level full factorial design experiment and a three factor Box-Behnken design were carried out. The goal was to establish a method to prepare N-sulfo, N-acetyl heparosan of the desired N-acetyl content, number average molecular weight, and in maximum yield by controlling the reactant concentrations, reaction time and reaction temperature. The response surface models obtained were used to predict the reaction conditions required to optimally prepare N-sulfo, N-acetyl heparosan from Escherichia coli generated heparosan starting material of different molecular weights.     

Metabolic engineering of Bacillus subtilis for biosynthesis of heparosan using heparosan synthase from Pasteurella multocida,PmHS1

Heparosan, the capsular polysaccharide discovered in many pathogenic bacteria, is a promising material for heparin preparation. In this study, the Pasteurella multocida heparosan synthase 1 (PmHS1) module was used to synthesize heparosan with controlled molecular weight, while tuaD/gtaB module or gcaD module was responsible for UDP-precursors production in Bacillus subtilis 168. After metabolic pathway optimization, the yield of heparosan was as high as 237.6 mg/L in strain containing PmHS1 module and tuaD/gtaB module, which indicated that these two modules were key factors in heparosan production. The molecular weight of heparosan varied from 39 to 53 kDa, which indicated that heparosan molecular weight could be adjusted by the amount of PmHS1 and the ratio of two UDP precursors. The results showed that it would be possible to produce safe heparosan with appropriate molecular weight which is useful in heparin production.

     

Ozonolysis of the double bond of the unsaturated uronate residue in low-molecular-weight heparin and K5 heparosan

Ozone is known to add across and cleave carbon–carbon double bonds. Ozonolysis is widely used for the preparation of pharmaceuticals, for bleaching substances and for killing microorganisms in air and water sources. Some polysaccharides and oligosaccharides, such as those prepared using chemical or enzymatic β-elimination, contain a site of unsaturation. We examined ozonolysis of low-molecular-weight heparins (LMWHs), enoxaparin and logiparin, and heparosan oligo- and polysaccharides for the removal of the nonreducing terminal unsaturated uronate residue. 1D ¹H NMR showed that these ozone-treated polysaccharides retained the same structure as the starting polysaccharide, except that the C4–C5 double bond in the nonreducing end unsaturated uronate had been removed. The anticoagulant activity of the resulting product from enoxaparin and logiparin was comparable to that of the starting material. These results demonstrate that ozonolysis is an important tool for the removal of unsaturated uronate residues from LMWHs and heparosan without modification of the core polysaccharide structure or diminution of anticoagulant activity. This reaction also has potential applications in the chemoenzymatic synthesis of bioengineered heparin from Escherichia coli-derived K5 heparosan.     

A purification process for heparin and precursor polysaccharides using the pH responsive behavior of chitosan

The contamination crisis of 2008 has brought to light several risks associated with use of animal tissue derived heparin. Because the total chemical synthesis of heparin is not feasible, a bioengineered approach has been proposed, relying on recombinant enzymes derived from the heparin/HS biosynthetic pathway and Escherichia coli K5 capsular polysaccharide. Intensive process engineering efforts are required to achieve a cost‐competitive process for bioengineered heparin compared to commercially available porcine heparins. Towards this goal, we have used 96‐well plate based screening for development of a chitosan‐based purification process for heparin and precursor polysaccharides. The unique pH responsive behavior of chitosan enables simplified capture of target heparin or related polysaccharides, under low pH and complex solution conditions, followed by elution under mildly basic conditions. The use of mild, basic recovery conditions are compatible with the chemical N‐deacetylation/N‐sulfonation step used in the bioengineered heparin process. Selective precipitation of glycosaminoglycans (GAGs) leads to significant removal of process related impurities such as proteins, DNA and endotoxins. Use of highly sensitive liquid chromatography‐mass spectrometry and nuclear magnetic resonance analytical techniques reveal a minimum impact of chitosan‐based purification on heparin product composition. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1348–1359, 2015     

途径优化强化枯草芽胞杆菌合成肝素前体

肝素前体是化学酶法合成肝素的起点,肝素前体的微生物高效合成具有重要意义。在已构建的产肝素前体的枯草芽胞杆菌((1.71±0.08)g/L)中,分析了UDP-葡萄糖醛酸(UDP-GlcUA)途径中关键酶基因(pgcA、gtaB、tuaD)以及UDP-乙酰氨基葡糖(UDP-GlcNAc)途径中关键酶基因(glmS、glmM、glmU)的过量表达对肝素前体产量及其分子量的影响。在此基础上,通过共表达tuaD、gtaB、glmU、glmM和glmS基因,摇瓶中肝素前体产量提高至(2.89±0.11)g/L,分子量为(75.90±1.18)kDa。通过在3 L发酵罐中进行补料分批发酵,肝素前体的产量最终积累到(7.25±0.36)g/L,分子量为(46.66±2.71)kDa,为工业化生产肝素奠定了基础。     

大肠杆菌K5产肝素前体heparosan的研究进展

肝素是一种被广泛临床应用的抗凝血药物多糖。Heparosan是某些细菌荚膜中的GAG成分,其二糖骨架结构与脊椎动物中的肝素类似,可以作为肝素和硫酸乙酰肝素的生物合成前体。本文综述了肝素及肝素前体heparosan的功能与应用,heparosan在大肠杆菌K5中合成转运相关酶的研究,以及发酵法生产heparosan的研究进展,并对其应用前景进行了展望。     

Production of N-sulfated polysaccharides using yeast-expressed N-deacetylase/N-sulfotransferase-1 (NDST-1)

Heparan sulfate/heparin N-deacetylase/N-sulfotransferase-1 (NDST-1) is a critical enzyme involved in heparan sulfate/heparin biosynthesis. This dual-function enzyme modifies the GlcNAc-GlcA disaccharide repeating sugar backbone to make N-sulfated heparosan. N-sulfation is an absolute requirement for the subsequent epimerization and O-sulfation steps in heparan sulfate/heparin biosynthesis. We have expressed rat liver (r) NDST-1 in Saccharomyces cerevisiae as a soluble protein. The yeast-expressed enzyme has both N-deacetylase and N-sulfotransferase activities. N-acetyl heparosan, isolated from Escherichia coli K5 polysaccharide, de-N-sulfated heparin (DNSH) and completely desulfated N-acetylated heparan sulfate (CDSNAcHS) are all good substrates for the rNDST-1. However, N-desulfated, N-acetylated heparin (NDSNAcH) is a poor substrate. The rNDST-1 was partially purified on heparin Sepharose CL-6B. Purified rNDST-1 requires Mn(2+) for its enzymatic activity, can utilize PAPS regenerated in vitro by the PAPS cycle (PAP plus para-nitrophenylsulfate in the presence of arylsulfotransferase IV), and with the addition of exogenous PAPS is capable of producing 60-65% N-sulfated heparosan from E. coli K5 polysaccharide or Pasteurella multocida polysaccharide.     

Chemoenzymatic synthesis with distinct Pasteurella heparosan synthases: monodisperse polymers and unnatural structures

Heparosan (-GlcUA-beta1,4-GlcNAc-alpha1,4-)(n) is a member of the glycosaminoglycan polysaccharide family found in the capsule of certain pathogenic bacteria as well as the precursor for the vertebrate polymers, heparin and heparan sulfate. The two heparosan synthases from the Gram-negative bacteria Pasteurella multocida, PmHS1 and PmHS2, were efficiently expressed and purified using maltose-binding protein fusion constructs. These relatively homologous synthases displayed distinct catalytic characteristics. PmHS1, but not PmHS2, was able to produce large molecular mass (100-800 kDa) monodisperse polymers in synchronized, stoichiometrically controlled reactions in vitro. PmHS2, but not PmHS1, was able to utilize many unnatural UDP-sugar analogs (including substrates with acetamido-containing uronic acids or longer acyl chain hexosamine derivatives) in vitro. Overall these findings reveal potential differences in the active sites of these two Pasteurella enzymes. In the future, these catalysts should allow the creation of a variety of heparosan and heparinoids with utility for medical applications.     

Heparosan Chain Characterization: Sequential Depolymerization of E. Coli K5 Heparosan by a Bacterial Eliminase Heparin Lyase III and a Bacterial Hydrolase Heparanase Bp to Prepare Defined Oligomers

Heparosan is a non-sulfated polysaccharide and potential applications include, chemoenzymatic synthesis of heparin and heparan sulfates. Heparosan is produced using microbial cells (natural producers or engineered cells). The characterization of heparosan isolated from both natural producers and engineered-cells are critical steps towards the potential applications of heparosan. Heparosan is characterized using 1) analysis of intact chain size and polydispersity, and 2) disaccharide composition. The current paper describes a novel method for heparosan chain characterization, using heparin lyase III (Hep-3, an eliminase from Flavobacterium heparinum) and heparanase Bp (Hep-Bp, a hydrolase from Burkholderia pseudomallei). The partial digestion of E. coli K5 heparosan with purified His-tagged Hep-3 results in oligomers of defined sizes. The oligomers (degree of polymerization from 2 to 8, DP2-DP8) are completely digested with purified GST-tagged Hep-Bp and analyzed using gel permeation chromatography. Hep-Bp specifically cleaves the linkage between d -glucuronic acid (GlcA) and N-acetyl-d -glucosamine (GlcNAc) but not the linkage between 4-deoxy-α-L-threo-hex-4-enopyranosyluronic acid (deltaUA) and GlcNAc, and results in the presence of a minor resistant trisaccharide (GlcNAc-GlcA-GlcNAc). This method successfully demonstrated the substrate selectivity of Hep-BP on heparosan oligomers. This analytical tool could be applied towards heparosan chain mapping and analysis of unnatural sugar moieties in the heparosan chain.     

Chromosome evolution of Escherichia coli Nissle 1917 for high-level production of heparosan

Heparosan is a crucial-polysaccharide precursor for the chemoenzymatic synthesis of heparin, a widely used anticoagulant drug. Presently, heparosan is mainly extracted with the potential risk of contamination from Escherichia coli strain K5, a pathogenic bacterium causing urinary tract infection. Here, a nonpathogenic probiotic, E. coli strain Nissle 1917 (EcN), was metabolically engineered to carry multiple copies of the 19-kb kps locus and produce heparosan to 9.1 g/L in fed-batch fermentation. Chromosome evolution driven by antibiotics was employed to amplify the kps locus, which governed the synthesis and export of heparosan from EcN at 21 mg L⁻¹ OD⁻¹. The average copy number of kps locus increased from 1 to 24 copies per cell, which produced up to 104 mg L^-1 OD⁻¹ of heparosan in the shaking flask cultures of engineered strains. The following in-frame deletion of recA stabilized the recombinant duplicates of chromosomal kps locus and the productivity of heparosan in continuous culture for at least 56 generations. Fed-batch fermentation of the engineered strain EcN8 was carried out to bring the yield of heparosan up to 9.1 g/L. Heparosan from the fermentation culture was further purified at a 75% overall recovery. The structure of purified heparosan was characterized and further modified by N-sulfotransferase with 3′-phosphoadenosine-5′-phosphosulfate as the sulfo-donor. The analysis of element composition showed that heparosan was N-sulfated by over 80%. These results indicated that duplicating large DNA cassettes up to 19-kb, followed by high-cell-density fermentation, was promising in the large-scale preparation of chemicals and could be adapted to engineer other industrial-interest bacteria metabolically.     

In vitro synthesis of heparosan using recombinant Pasteurella multocida heparosan synthase PmHS2

In vertebrates and bacteria, heparosan the precursor of heparin is synthesized by glycosyltransferases via the stepwise addition of UDP-N-acetylglucosamine and UDP-glucuronic acid. As heparin-like molecules represent a great interest in the pharmaceutical area, the cryptic Pasteurella multocida heparosan synthase PmHS2 found to catalyze heparosan synthesis using substrate analogs has been studied. In this paper, we report an efficient way to purify PmHS2 and to maintain its activity stable during 6 months storage at −80 °C using His-tag purification and a desalting step. In the presence of 1 mM of each nucleotide sugar, purified PmHS2 synthesized polymers up to an average molecular weight of 130 kDa. With 5 mM of UDP-GlcUA and 5 mM of UDP-GlcNAc, an optimal specific activity, from 3 to 6 h of incubation, was found to be about 0.145 nmol/μg/min, and polymers up to an average of 102 kDa were synthesized in 24 h. In this study, we show that the chain length distribution of heparosan polymers can be controlled by change of the initial nucleotide sugar concentration. It was observed that low substrate concentration favors the formation of high molecular weight heparosan polymer with a low polydispersity while high substrate concentration did the opposite. Similarities in the polymerization mechanism between PmHS2, PmHS1, and PmHAS are discussed.     

Identification of a distinct, cryptic heparosan synthase from Pasteurella multocida types A, D, and F

The extracellular polysaccharide capsules of Pasteurella multocida types A, D, and F are composed of hyaluronan, N-acetylheparosan (heparosan or unsulfated, unepimerized heparin), and unsulfated chondroitin, respectively. Previously, a type D heparosan synthase, a glycosyltransferase that forms the repeating disaccharide heparosan backbone, was identified. Here, a approximately 73% identical gene product that is encoded outside of the capsule biosynthesis locus was also shown to be a functional heparosan synthase. Unlike PmHS1, the PmHS2 enzyme was not stimulated greatly by the addition of an exogenous polymer acceptor and yielded smaller- molecular-weight-product size distributions. Virtually identical hssB genes are found in most type A, D, and F isolates. The occurrence of multiple polysaccharide synthases in a single strain invokes the potential for capsular variation.