Chemical treatment of Escherichia coli. II. Direct extraction of recombinant protein from cytoplasmic inclusion bodies in intact cells

A method is presented for the direct extraction of the recombinant protein Long-R3-IGF-I from inclusion bodies located in the cytoplasm of intact Escherichia coli cells. Chemical treatment with 6M urea, 3 mM EDTA, and 20 mM dithiothreitol (DTT) at pH 9.0 proved an effective combination for extracting recombinant protein from intact cells. Comparable levels of Long-R3-IGF-I were recovered by direct extraction as achieved by in vitro dissolution following mechanical disruption. However, the purity of directly extracted recombinant protein was lower due to contamination by bacterial cell components. The kinetics of direct extraction are described using a first-order equation with the time constant of 3 min. Urea appears important for permeabilization of the cell and dissolution of the inclusion body. Conversely, EDTA is involved in permeabilization of the cell wall and DTT enhances protein release. pH proved to be important with lower levels of protein release achieved at low pH values (<9). Cell concentration also had a minor effect on Long-R3-IGF-I release and caused an observable increase in viscosity. Advantages of the direct extraction method include its speed, simplicity, and efficiency at releasing product.     

The mechanism of carbonate killing of Escherichia coli

AIMS: To define the mechanism of carbonate killing in Escherichia coli. METHODS AND RESULTS: Sodium carbonate (150 mM) and ethylenediaminetetracetic acid (EDTA, 60 mM) both killed E. coli K-12 when the pH was 8.5, but ammonium chloride (150 mM) was ineffective. EDTA was a 5-fold more potent agent than carbonate, but some of this difference could be explained by ionization. At pH 8.5, only 1.6% of the carbonate is CO(-2), but nearly 100% of the EDTA is EDTA(-2). CONCLUSION: As carbonate and EDTA had similar effects on viability, cellular morphology, protein release and enzymatic activities, the antibacterial activity of carbonate seems to be mediated by divalent metal binding. SIGNIFICANCE AND IMPACT OF THE STUDY: Cattle manure is often used as a fertilizer, and E. coli from manure can migrate through the soil into water supplies. Previous methods of eradicating E. coli were either expensive or environmentally unsound. However, cattle manure can be treated with carbonate to eliminate E. coli, and the cost of this treatment is less than $0.03 per cow per day.     

Selective precipitation of DNA by spermine during the chemical extraction of insoluble cytoplasmic protein.

The direct chemical extraction of recombinant L1 protein (the major capsid protein of human papillomavirus type 16) from the cytoplasm of E. coli HMS174(DE3) has recently been demonstrated at high cell density (to OD(600) = 160) without the use of reducing agent (1). Coextraction of DNA at high concentration prevents direct coupling to postextraction recovery operations including expanded bed adsorption. In this study, spermine is used to selectively precipitate DNA during chemical extraction. Highly efficient and selective DNA precipitation was achieved. An approximate 10-fold increase in the specific spermine concentration (mg of spermine/mg of DNA) was required to precipitate DNA when 8 M urea was added to the extraction buffer. EDTA (3 mM), required for effective chemical extraction, does not significantly inhibit DNA precipitation. Precipitation selectivity was demonstrated in a bovine serum albumin spiking test, with almost complete recovery of the spiked protein. During studies on the direct extraction of L1 protein from cells at OD(600) = 80, high DNA removal efficiency (>85%) and negligible L1 protein coprecipitation were achieved. This selective precipitation technique simply requires the addition of spermine to the chemical extraction buffer and therefore does not increase technique complexity. This modification enhances the method's general applicability and enables direct coupling to downstream recovery units following chemical extraction at high cell and product concentrations.     

Chemical treatment of Escherichia coli: 3. Selective extraction of a recombinant protein from cytoplasmic inclusion bodies in intact cells

In previous parts of this study we developed procedures for the high‐efficiency chemical extraction of soluble and insoluble protein from intact Escherichia coli cells. Although high yields were obtained, extraction of recombinant protein directly from cytoplasmic inclusion bodies led to low product purity due to coextraction of soluble contaminants. In this work, a two‐stage procedure for the selective extraction of recombinant protein at high efficiency and high purity is reported. In the first stage, inclusion‐body stability is promoted by the addition of 15 mM 2‐hydroxyethyldisulfide (2‐HEDS), also known as oxidized β‐mercaptoethanol, to the permeabilization buffer (6 M urea + 3 mM ethylenediaminetetraacetate [EDTA]). 2‐HEDS is an oxidizing agent believed to promote disulfide bond formation, rendering the inclusion body resistant to solubilization in 6 M urea. Contaminating proteins are separated from the inclusion‐body fraction by centrifugation. In the second stage, disulfide bonds are readily eliminated by including reducing agent (20 mM dithiothreitol [DTT]) into the permeabilization buffer. Extraction using this selective two‐stage process yielded an 81% (w/w) recovery of the recombinant protein Long‐R³‐IGF‐I from inclusion bodies located in the cytoplasm of intact E. coli, at a purity of 46% (w/w). This was comparable to that achieved by conventional extraction (mechanical disruption followed by centrifugation and solubilization). A pilot‐scale procedure was also demonstrated using a stirred reactor and diafiltration. This is the first reported study that achieves both high extraction efficiency and selectivity by the chemical treatment of cytoplasmic inclusion bodies in intact bacterial cells. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 62: 455–460, 1999.     

Overexpression, purification and characterization of the catalytic component of Oplophorus luciferase in the deep-sea shrimp, Oplophorus gracilirostris

The luciferase secreted by the deep-sea shrimp Oplophorus consists of 19 and 35kDa proteins. The 19-kDa protein (19kOLase), the catalytic component of luminescence reaction, was expressed in Escherichia coli using the cold-shock inducted expression system. 19kOLase, expressed as inclusion bodies, was solubilized with 6M urea and purified by urea-nickel chelate affinity chromatography. The yield of 19kOLase was 16 mg from 400 ml of cultured cells. 19kOLase in 6M urea could be refolded rapidly by dilution with 50mM Tris-HCl (pH 7.8)-10mM EDTA, and the refolded protein showed luminescence activity. The luminescence properties of refolded 19kOLase were characterized, in comparison with native Oplophorus luciferase. Luminescence intensity with bisdeoxycoelenterazine as a substrate was stimulated in the presence of organic solvents. The 19kOLase is a thermolabile protein and is 98 % inhibited by 1muM Cu2+. The cysteine residue of 19kOLase is not essential for catalysis of the luminescence reaction.     

Expression, purification, and in vitro refolding of a humanized single-chain Fv antibody against human CTLA4 (CD152)

A human-derived single-chain Fv (scFv) antibody fragment specific against human CTLA4 (CD152) was produced at high level in Escherichia coli. The scFv gene was cloned from a phagemid to the expression vector pQE30 with a N-terminal 6His tag fused in-frame, and expressed as a 29 kDa protein in E. coli as inclusion bodies. The inclusion body of scFv was isolated from E. coli lysate, solubilized in 8M urea with 10mM dithiothreitol, and purified by ion-exchange chromatography. Method for in vitro refolding of the scFv was established. The effects of refolding buffer composition, protein concentration and temperature on the refolding yield were investigated. The protein was renatured finally by dialyzing against 3mM GSH, 1mM GSSG, 150 mM NaCl, 1M urea, and 50 mM Tris-Cl (pH 8.0) for 48 h at 4 degrees C, and then dialyzed against phosphate-buffered saline (pH 7.4) to remove remaining denaturant. This refolding protocol generated up to a 70% yield of soluble protein. Soluble scFv was characterized for its specific antigen-binding activity by indirect cellular ELISA. The refolded scFv was functionally active and was able to bind specifically to CTLA4 (CD152). The epitopes recognized by refolded anti-CTLA4 scFv do not coincide with those epitopes recognized by CD80/CD86.     

Improvement of the extraction of penicillin acylase from Escherichia coli cells by a combined use of chemical methods

Several techniques for protein extraction were tested for recovering penicillin acylase from a recombinant strain of Escherichia coli. These techniques include chemical [guanidine hydrochloride, Triton X-100, ethylenediaminetetraacetic acid (EDTA), ethanol/toluene], physical (sonication, freeze-and-thawing), and enzymatic (lysozyme) treatments. Best results were obtained with the combined use of guanidine and EDTA. This extraction procedure was optimized, and it was found that 95% of the enzyme was extracted after a 10 m/M EDTA plus 10 mM guanidine treatment at room temperature for 10 h. The purification factor was 25 when compared to disruption by sonication. This extraction method could avoid purification steps for particular applications. (c) 1994 John Wiley & Sons, Inc.     

Flow analysis coupled with PQC/DNA biosensor for assay of E. coli based on detecting DNA products from PCR amplification

A flow-through PQC/DNA biosensor system is developed by combining sequential flow polymerase chain reaction (PCR) products denaturing prior to piezoelectric quartz crystal (PQC) detection via hybridization of ssDNA. The PQC/DNA biosensor is fabricated based on complex formation of neutravidin/biotinylated probe in 0.2M NaCl in TE buffer (10mM Tris, 1mM EDTA, pH 7.5). Results show that the coating fabricated provides a desirable quality with satisfactory performance. Its application for Escherichia coli detection under controlled flow at 0.02 mL/min for denaturing PCR products and 10 mL/min for transferring solution between reactors and delivering samples to detector to reduce rehybridization leads to significant improvement in repeatability (R.S.D.<6%, n=5) and sensitivity (DeltaF=34 Hz/1000 E. coli cells) as compared to existing manual method (R.S.D.=19%, n=5 and DeltaF=26 Hz/1000 E. coli cells, respectively). Down to 23 E. coli cells are detected, satisfying the HKEPD requirements for E. coli count in beach water.     

Production of enzymatically active ketosteroid isomerase following insoluble expression in Escherichia coli

Enzymatically active Delta(5)-3-ketosteroid isomerase (KSI) protein with a C-terminus his(6)-tag was produced following insoluble expression using Escherichia coli. A simple, integrated process was used to extract and purify the target protein. Chemical extraction was shown to be as effective as homogenization at releasing the inclusion body proteins from the bacterial cells, with complete release taking less than 20 min. An expanded bed adsorption (EBA) column utilizing immobilized metal affinity chromatography (IMAC) was then used to purify the denatured KSI-(His(6)) protein directly from the chemical extract. This integrated process greatly simplifies the recovery and purification of inclusion body proteins by removing the need for mechanical cell disruption, repeated inclusion body centrifugation, and difficult clarification operations. The integrated chemical extraction and EBA process achieved a very high purity (99%) and recovery (89%) of the KSI-(His(6)), with efficient utilization of the adsorbent matrix (9.74 mg KSI-(His(6))/mL adsorbent). Following purification the protein was refolded by dilution to obtain the biologically active protein. Seventy-nine percent of the expressed KSI-(His(6)) protein was recovered as enzymatically active protein with the described extraction, purification, and refolding process. In addition to demonstrating the operation of this intensified inclusion body process, a plate-based concentration assay detecting KSI-(His(6)) is validated. The intensified process in this work requires minimal optimization for recovering novel his-tagged proteins, and further improves the economic advantage of E. coli as a host organism.     

A new study of cell disruption to release recombinant thermostable enzyme from Escherichia coli by thermolysis

Extraction of intracellular protein from Escherichia coli is traditionally achieved by mechanical, chemical or enzymatic disruption technology. In this study, a novel thermolysis method was used to disrupt E. coli cells to release a recombinant thermostable esterase. We found that heat treatment of E. coli was highly effective to destroy the integrity of bacterial cell walls and release the recombinant hyperthermophilic esterase at temperatures above 60 degrees C. The effects of temperature, pH and cell concentration on the efficiency of cell disruption were examined. The most effective temperature for cell disruption was at 80 degrees C. The pH and cell concentration had only minor effect on the release of the hyperthermophilic esterase. In addition, we found that the hyperthermophilic esterase could be purified at the early stage of the thermolysis, which is a major advantage of the thermolysis method. Finally, a comparison between thermolysis and traditional methods for the disruption of cells and the release of the thermostable enzyme was made.     

Conversion of native oligomeric to a modified monomeric form of human C-reactive protein

C-reactive protein (CRP) is a pentameric oligoprotein composed of identical 23 kD subunits which can be modified by urea-chelation treatment to a form resembling the free subunit termed modified CRP (mCRP). mCRP has distinct physicochemical, antigenic, and biologic activities compared to CRP. The conditions under which CRP is converted to mCRP, and the molecular forms in the transition, are important to better understand the distinct properties of mCRP and to determine if the subunit form can convert back to the pentameric native CRP form. This study characterized the antigenic and conformational changes associated with the interconversion of CRP and mCRP. The rate of dissociation of CRP protomers into individual subunits by treatment in 8 M urea–10 mM EDTA solution was rapid and complete in 2 min as assayed by an enzyme-linked immunofiltration assay using monoclonal antibodies specific to the mCRP. Attempts to reconstitute pentameric CRP from mCRP under renaturation conditions were unsuccessful, resulting in a protein retaining exclusively mCRP characteristics. Using two-dimensional urea gradient gel electrophoresis, partial rapid unfolding of the pentamer occurred above 3 M urea, a subunit dissociation at 6 M urea, and further subunit unfolding at 6–8 M urea concentrations. The urea gradient electrophoresis results suggest that there are only two predominant conformational states occurring at each urea transition concentration. Using the same urea gradient electrophoresis conditions mCRP migrated as a single molecular form at all urea concentrations showing no evidence for reassociation to pentameric CRP or other aggregate form. The results of this study show a molecular conversion for an oligomeric protein (CRP) to monomeric subunits (mCRP) having rapid forward transition kinetics in 8 M urea plus chelator with negligible reversibility.     

Equilibrium, kinetic, and footprinting studies of the Tus-Ter protein-DNA interaction.

Arrest of DNA replication in the terminus region of the Escherichia coli chromosome is mediated by protein-DNA complexes composed of the Tus protein and 23 base pair sequences generically called Ter sites. We have characterized the in vitro binding of purified Tus protein to a 37-base pair oligodeoxyribonucleotide containing the TerB sequence. The measured equilibrium binding constant (KD) for the chromosomal TerB site in KG buffer (50 mM Tris-Cl, 150 mM potassium glutamate, 25 degrees C, pH 7.5, 0.1 mM dithiothreitol, 0.1 mM EDTA, and 100 micrograms/ml bovine serum albumin) was 3.4 x 10(-13) M. Kinetic measurements in the same buffer revealed that the Tus-TerB complex was very stable, with a half-life of 550 min, a dissociation rate constant of 2.1 x 10(-5) s-1, and an association rate constant of 1.4 x 10(8) M-1 s-1. Similar measurements of Tus protein binding to the TerR2 site of the plasmid R6K showed an affinity 30-fold lower than the Tus-TerB interaction. This difference was due primarily to a more rapid dissociation of the Tus-TerR2 complex. Using standard chemical modification techniques, we also examined the DNA-protein contacts of the Tus-TerB interaction. Extensive contacts between the Tus protein and the TerB sequence were observed in the highly conserved 11 base-pair "core" sequence common to all identified Ter sites. In addition, protein-DNA contact sites were observed in the region of the Ter site where DNA replication is arrested. Projection of the footprinting data onto B-form DNA indicated that the majority of the alkylation interference and hydroxyl radical-protected sites were arranged on one face of the DNA helix. We also observed dimethyl sulfate protection of 2 guanine residues on the opposite side of the helix, suggesting that part of the Tus protein extends around the double helix. The distribution of contacts along the TerB sequence was consistent with the functional polarity of the Tus-Ter complex and suggested possible mechanisms for the impediment of protein translocation along DNA.     

Initial protein concentration and residual denaturant concentration strongly affect the batch refolding of hen egg white lysozyme

The effects of several variables on the refolding of hen egg white lysozyme have been studied. Lysozyme was denatured in both urea, and guanidine hydrochloride (GuHCl), and batch refolded by dilution (100 to 1000 fold) into 0.1M Tris-HCl, pH 8.2, 1 mM EDTA, 3 mM reduced glutathione and 0.3 mM oxidised glutathione. Refolding was found to be sensitive to temperature, with the highest refolding yield obtained at 50°C. The apparent activation energy for lysozyme refolding was found to be 56 kJ/mol. Refolding by dilution results in low concentrations of both denaturant and reducing agent species. It was found that the residual concentrations obtained during dilution (100-fold dilution: [GuHCl]=0.06 mM, [DTT]=0.15 mM) were significant and could inhibit lysozyme refolding. This study has also shown that the initial protein concentration (1–10 mg/mL) that is refolded is an important parameter. In the presence of residual GuHCl and DTT, higher refolding yields were obtained when starting from higher initial lysozyme concentrations. This trend was reversed when residual denaturant components were removed from the refolding buffer.     

Active papain renatured and processed from insoluble recombinant propapain expressed in Escherichia coli.

For the first time the pro-form of a recombinant cysteine proteinase has been expressed at a high level in Escherichia coli. This inactive precursor can subsequently be processed to yield active enzyme. Sufficient protein can be produced using this system for X-ray crystallographic structure studies of engineered proteinases. A cDNA clone encoding propapain, a precursor of the papaya proteinase, papain, was expressed in E. coli using a T7 polymerase expression system. Insoluble recombinant protein was solubilized in 6 M guanidine hydrochloride and 10 mM dithiothreitol, at pH 8.6. A protein-glutathione mixed disulphide was formed by dilution into oxidized glutathione and 6 M GuHCl, also at pH 8.6. Final refolding and disulphide bond formation was induced by dilution into 3 mM cysteine at pH 8.6. Renatured propapain was processed to active papain at pH 4.0 in the presence of excess cysteine. Final processing could be inhibited by the specific cysteine proteinase inhibitors E64 and leupeptin, but not by pepstatin, PMSF or EDTA. This indicates that final processing was due to a cysteine proteinase and suggests that an autocatalytic event is required for papain maturation.     

N-Glycosidase activity in extracts of Bacillus subtilis and its inhibition after infection with bacteriophage PBS2.

We have detected in crude extracts of Bacillus subtilis an N-glycosidase activity which catalyzes the release of free uracil from DNA of the subtilis phage PBS2 labeled with [3H]uridine. This DNA contains deoxyuridine instead of thymidine. The enzyme is active in the presence of 1.0 mM EDTA and under these conditions Escherichia coli or T7 DNA labeled with [3H]thymidine is not degraded to labeled acid-soluble products. The activity resembles an N-glycosidase from E. coli which releases free uracil from DNA containing deaminated cytosine residues. Both enzymes in crude extracts are active in the presence of EDTA, do not require dialyzable co-factors, and have the same pH optimum. They differ in that the enzyme from E. coli is more sensitive to heat, sulfhydryl reagents, and salt. The enzyme from B. subtilis is inactive on DNA containing 5-bromouracil or hydroxymethyluracil. Extracts of PBS2-infected B. subtilis lose the N-glycosidase activity within 4 min after infection and contain a factor that inhibits the N-glycosidase activity within 4 min after infection and contain a factor that inhibits the N-glycosidase activity in extracts of uninfected cells in vitro.     

Pro-subtilisin E: purification and characterization of its autoprocessing to active subtilisin E in vitro

The formation of active subtilisin E from pro-subtilisin E requires the removal of the N-terminal pro-sequence of 77 residues. Pro-subtilisin E produced in Escherichia coli using a pINIII-ompA vector was first extracted with 6 M guanidine-HCl and 5 M urea and purified to homogeneity in the presence of 5 M urea. Upon drop dialysis against 0.2 M sodium phosphate buffer (pH 6.2), the purified pro-subtilisin in 5 M urea was processed to active subtilisin of which the N-terminal sequence and migration in SDS-polyacrylamide gel electrophoresis were identical to those of authentic active subtilisin E. This process was found to be very sensitive to the ionic strengths and anions used. Under the optimum conditions (dialysis against 0.5 M (NH4)2SO4 and 1 mM CaCl2 in 10 mM Tris-HCl buffer (pH 7.0) at 4 degrees C for 1 h), approximately 20% of pro-subtilisin E was converted to active subtilisin E. The activation process was not inhibited by Streptomyces subtilisin inhibitor, and pro-subtilisin E in which the active site was mutated (Asp32 to Asn) was unable to be processed under the optimum conditions. These results confirmed the previous hypothesis that the processing of pro-subtilisin occurs by an intramolecular, autoprocessing mechanism.     

Subunit association and side-chain reactivities of bovine erythrocyte superoxide dismutase in denaturing solvents.

The copper- and zinc-containing superoxide dismutase of bovine erythrocytes retains its native molecular weight of 32 000 in 8.0 M urea for at least 72 h at 25 degrees C, as evidenced by sedimentation equilibrium analysis. Subsequent to prolonged exposure to urea, the dimeric enzyme could be dissociated by sodium dodecyl sulfate in the absence of reductants, indicating the absence of unnatural disulfide cross-links. The sulfhydryl group of cysteine-6 was unreactive toward 5,5'-dithiobis(2-nitrobenzoic acid) or bromoacetic acid in both neutral buffer and 8.0 M urea. The histidine residues of the enzyme were resistant to carboxymethylation in neutral buffer and 8.0 M urea. However, when the enzyme was exposed to bromoacetic acid in the presence of 6.0 M guanidinium chloride and 1 mM (ethylenedinitriol)tetraacetic acid (EDTA), both sulfhydryl and histidine alkylation were observed. Guanidinium chloride (6.0 M) increased the reactivity of the sulfhydryl group of cysteine-6 and allowed the oxidative formation of disulfide-bridged dimers. This was prevented by 1 mM EDTA. It follows that 8.0 M urea neither dissociates the native enzyme into subunits nor produces a conformation detectably different than that possessed under native conditions.     

Combined chemical and mechanical processes for the disruption of bacteria.

Mechanical cell disruption by high pressure homogenisation or high speed bead mills is currently the general method of choice for the large scale disruption of micro-organisms; however, deleterious effects include the high energy requirement, the need for efficient cooling to prevent the excessive heating of the product and the micronisation of cell debris. Certain chemical treatments for microbial cell disruption alter the permeability of bacteria and yeasts, allowing partial release of soluble products. Such treatments are insufficient for the recovery of granular intracellular products. As cell wall strength has been cited as a major factor influencing the requirements for efficient mechanical disruption, the use of chemical pretreatment to decrease cell wall strength prior to mechanical breakage by homogenisation has been considered. The following treatments were shown to increase the sensitivity of the Gram-negative bacterium, Alcaligenes eutrophus, to disruption: alkaline pH shock, the addition of an anionic detergent, increase of the monovalent cation concentration, the addition of EDTA and enzymic lysis by lysozyme. These pretreatments allow equivalent disruption to be achieved at lower operating pressures or fewer passes through the homogeniser. Alkaline pH pretreatment at pH 10.5 allowed a 37.5% increase in soluble protein release on subsequent homogenisation. An increase of some 30% in soluble protein release was found following prior addition of 0.137 M monovalent cations (Na+ or K+) at 60 degrees C. Treatment with an anionic detergent showed a considerable decrease in the number of passes required through the homogeniser. Maximum cell rupture can thus be accomplished at reduced energy inputs.     

Physiological characteristics of recombinant Escherichia coli cells displaying poly-His peptides

Using the Escherichia coli OmpC protein as an anchoring motif, four different poly-His units (1, 2, 3 and 6 copies of 6-His) were displayed on the seventh loop of the OmpC. Recombinant E. coli strains displaying 1, 3 or 6 copies of poly-His became much more sensitive to SDS (0.1%, w/v) and EDTA (2 mM) compared with control strains. However, recombinant E. coli cells displaying 2 copies of poly-His were resistant to SDS and EDTA; greater than 70% and 90% of cells maintained cell integrity after 60 min treatment with SDS and EDTA, respectively, suggesting its usefulness as a whole cell biosorbent.     

Cloning, high-level expression, single-step purification, and binding activity of His6-tagged recombinant type B botulinum neurotoxin heavy chain transmembrane and binding domain

Botulinum neurotoxins (BoNTs) are highly potent toxins that inhibit neurotransmitter release from peripheral cholinergic synapses and associate with infant botulism. BoNT is a approximately 150kDa protein, consisting of a binding/translocating heavy chain (HC; 100kDa) and a toxifying light chain (LC; 50kDa) linked through a disulfide bond. C-terminal half of the heavy chain is binding domain, and N-terminal half of the heavy chain is translocation domain that includes transmembrane domain. A functional botulinum neurotoxin type B heavy chain transmembrane and binding domain (Ile 624-Glu 1291) has been cloned into a bacterial expression vector pET 15b and produced as an N-terminally six-histidine-tagged fusion protein (BoNT/B HC TBD). (His(6))-BoNT/B HC TBD was highly expressed in Escherichia coli BL21-CodonPlus (DE3)-RIL and isolated from the E. coli inclusion bodies. After solubilizing the purified inclusion bodies with 6M guanidine-HCl in the presence of 10mM beta-mercaptoethanol, the protein was purified and refolded in a single step on Ni(2+) affinity column by removing beta-mercaptoethanol first, followed by the removal of urea. The purified protein was determined to be 98% pure as assessed by SDS-polyacrylamide gel. (His(6))-BoNT/B HC TBD retained binding to synaptotagmin II, the receptor of BoNT/B, which was confirmed by immunological dot blot assay, also to ganglioside, which was investigated using enzyme-linked immunosorbent assay.