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.     

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.     

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.     

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.

     

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。     

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.     

Nuclear magnetic resonance quantification for monitoring heparosan K5 capsular polysaccharide production

Traditional chromatographic quantification methods for heparosan produced from the Escherichia coli K5 strain rely on extensive purification requiring laborious sample preparation. These methods are time-consuming, often resulting in sample loss during purification, and thus might not accurately reflect the amount of heparosan in the original mixture. A simple, sensitive ¹H nuclear magnetic resonance (NMR) quantification method that directly quantifies heparosan K5 polysaccharide present in E. coli fermentation supernatant is described.     

Escherichia coli K5 heparosan fermentation and improvement by genetic engineering

N-acetyl heparosan is the precursor for the biosynthesis of the important anticoagulant drug heparin. The E. coli K5 capsular heparosan polysaccharide provides a promising precursor for in vitro chemoenzymatic production of bioengineered heparin. This article explores the improvements of heparosan production for bioengineered heparin by fermentation process engineering and genetic engineering.     

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.     

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.     

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.     

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.     

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.     

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.     

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.     

Influence of the culture conditions on extracellular lyase activity related to K5 polysaccharide

The K5 capsular polysaccharide antigen of some Escherichia coli strains is the non-sulphated precursor in heparin biosynthesis. It is composed by two components, 16000 and 1500 Da, whose ratio depends on the activity of the extracellular form of a lyase synthesized by the same K5 producer strain. The lyase activity on the K5 chain size was greatly influenced by the medium composition employed for the lyase production. The control of lyase activity results in defined ratios of the two components in the K5 polysaccharide that is suitable for the semisynthetic production of heparin-like molecules.     

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。     

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.     

Extracellular K5 polysaccharidic antigen recovery performed by different cell separation technologies

The K5 polysaccharidic antigen obtainable from a strain of Escherichia coli is the non-sulphated precursor in heparin biosynthesis; K5 is composed by two components, 16000 and 1500 Da, their ratio depending on the fermentation conditions. In this study an assessment was made of how various cell-culture filtrate separation technologies affected the components themselves and their ratio. A dynamic membrane filtration technology, a tubular ceramic module for tangential flow microfiltration and the standard discontinuous centrifugation were comparatively employed to perform the separation. Experiments carried out on E. coli cultures containing the two components in different ratios showed that the DMF system is a suitable technology for K5 isolation.