Refolding and purification of Zymomonas mobilis levansucrase produced as inclusion bodies in fed-batch culture of recombinant Escherichia coli

Zymomonas mobilis levansucrase was overproduced by the fed-batch culture of recombinant Escherichia coli harboring a novel expression system that is constitutively expressed by the promoter from the Rahnella aquatilis levansucrase gene. Most of the levansucrase was produced as inclusion bodies in the bacterial cytoplasm, accounting for approximately 20% of the total cellular protein. Refolding after complete denaturation by high concentrations of urea or guanidine hydrochloride was not successful, resulting in large amounts of insoluble aggregates. During the development of the refolding method, it was found that direct solubilization of the inclusion bodies with Triton X-100 reactivated the enzyme, with a considerable refolding efficiency. About 65% of inclusion body levansucrase was refolded into active levansucrase in the renaturation buffer containing 4% (v/v) Triton X-100. The in vitro refolded enzyme was purified to 95% purity by single-step DEAE-Sepharose ion exchange chromatography. Triton X-100 was removed by this ion exchange chromatography.     

Cloning and purification of functionally active Fas ligand interfering protein (FIP) expressed in Escherichia coli

This report presents purification and characterization of the extracellular domain of rat Fas protein, called FIP (FasL interfering protein), expressed as inclusion bodies in Escherichia coli. FIP was extracted from the inclusion bodies, solubilized with 8 M urea, purified by a single-step immobilized metal ion (Ni(2+)) affinity chromatography and refolded. SDS/PAGE and mass spectrometry analysis of the purified protein verified its purity. Fluorescence spectrum analysis showed that the refolding procedure caused structural changes which presumably might have led to oligomerization. The purified FIP has biological activities: it binds specifically soluble Fas ligand and protects human Jurkat lymphocytes against FasL-dependent apoptosis. This efficient procedure of FIP expression in E. coli and renaturation may be useful for production of therapeutically important proteins.     

Expression, single-step purification, and matrix-assisted refolding of a maize cytokinin glucoside-specific beta-glucosidase.

Availability of highly purified native beta-glucosidase Zm-p60.1 in milligram quantities was a basic requirement for analysis of structure-function relationships of the protein. Therefore, Zm-p60.1 was overexpressed to high levels as a fusion protein with a hexahistidine tag, (His)(6)Zm-p60.r, in Escherichia coli, resulting, however, in accumulation of most of the protein in insoluble inclusion bodies. Native (His)(6)Zm-p60.r was then purified either from the bacterial lysate soluble fraction or from inclusion bodies. In the first case, a single-step purification under native conditions based on immobilized metal affinity chromatography (IMAC) was developed. In the second case, a single-step purification protocol under denaturing conditions followed by IMAC-based matrix-assisted refolding was elaborated. The efficiency of the native protein purification from soluble fraction of bacterial homogenate was compared to the feasibility of purification and renaturation of the protein from inclusion bodies. Gain of authentic biological activity and quaternary structure after the refolding process was confirmed by K(m) determination and electrophoretic mobility under native conditions. The yield of properly refolded protein was assessed based on the specific activity of the refolded product.     

Refolding and Purification of Zymomonas mobilis Levansucrase Produced as Inclusion Bodies in Fed-Batch Culture of Recombinant Escherichia coli

Zymomonas mobilis levansucrase was overproduced by the fed-batch culture of recombinant Escherichia coli harboring a novel expression system that is constitutively expressed by the promoter from the Rahnella aquatilis levansucrase gene. Most of the levansucrase was produced as inclusion bodies in the bacterial cytoplasm, accounting for approximately 20% of the total cellular protein. Refolding after complete denaturation by high concentrations of urea or guanidine hydrochloride was not successful, resulting in large amounts of insoluble aggregates. During the development of the refolding method, it was found that direct solubilization of the inclusion bodies with Triton X-100 reactivated the enzyme, with a considerable refolding efficiency. About 65% of inclusion body levansucrase was refolded into active levansucrase in the renaturation buffer containing 4% (v/v) Triton X-100. The in vitro refolded enzyme was purified to 95% purity by single-step DEAE–Sepharose ion exchange chromatography. Triton X-100 was removed by this ion exchange chromatography.     

Expression, purification, and characterization of an immunotoxin containing a humanized anti-CD25 single-chain fragment variable antibody fused to a modified truncated Pseudomonas exotoxin A

Vascular leak syndrome (VLS) is the major dose-limiting toxicity of immunotoxin therapy. In our previous study, a modified PE38KDEL, denoted PE38KDELKQK, was engineered to eliminate VLS. The PE38KDELKQK-based immunotoxin has been proved to retain potent anti-tumor activity but with a remarkable attenuation in VLS. In the present study, we have constructed and expressed a recombinant immunotoxin CD25-PE38KDELKQK containing humanized anti-CD25 single-chain antibody (scFv) genetically fused to PE38KDELKQK in Escherichia coli. After washing with buffer containing 2 M urea, the purity of inclusion body was about 82%. The denatured inclusion bodies were refolded on-column in Tris buffer (pH 8.0) containing 4mM of GSH and 1 mM of GSSG using a gradient of decreasing urea. We found that the presence of GSH/GSSG (4:1) in the on-column refolding buffer was important for efficient refolding. In addition, slow flow rate was another important factor could increase refolding. Under these conditions, the activity of the refolded protein could reach about 90% of that of the native protein. The refolded proteins were purified to homogeneity ( approximately 95% purity) by a combination of His-Ni(2+) metal affinity chromatography and gel filtration chromatography. The in vitro cytotoxicity assay indicated the purified immunotoxin CD25-PE38KDELKQK had specific cytotoxicity to CD25-positive leukemic cells comparable to wild-type CD25-PE38KDEL (wt). In contrast, CD25-PE38KDELKQK was shown to be much weaker in inducing VLS in mice than wt. The protein expression, purification, and refolding system established in this paper is important for further study on immunotoxin CD25-PE38KDELKQK.     

RGD-葡激酶的凝胶过滤层析法复性及其纯化

构建的溶栓和抗栓双重功能的RGD-葡激酶突变体(RGD-Sak)在大肠杆菌中高表达,目的蛋白质以包涵体形式存在。为获得有活性的蛋白质,需要对包涵体进行变复性。利用凝胶层析方法对包涵体中RGD-Sak进行复性,并与稀释复性法进行比较,发现凝胶柱复性方法具有操作周期短、简便、成本低而高效等优点。复性后蛋白质用Q-Sepharose FF离子交换进一步纯化,纯度达95%,酪蛋白凝胶板活性测定表明两种复性法得到的蛋白质比活性相当。圆二色谱测定显示两种复性法得到的蛋白质的二级结构成份和谱形一致,说明在两种复性过程中完成了RGD-Sak分子的正确折叠。     

Renaturation, purification and characterization of streptokinase expressed as inclusion body in recombinant E. coli

Recombinant protein purification is facilitated using high expression systems which produce larger quantities of streptokinase protein as inclusion bodies. As the accumulation of active streptokinase is toxic to the host cells, we have optimized the conditions to achieve large amounts of streptokinase in the form of inclusion bodies. The solubility and yield of pure protein are highly dependent on various combinations of chemical additives, ionic and non-ionic detergents and salts, with solubilizing agents followed by refolding of denatured protein into active form. As the extraction of the purified streptokinase from inclusion bodies requires denaturation and a subsequent refolding step, careful balancing steps were needed to develop under different controlled conditions. Here the purified fragments of refolded proteins were screened to select the conditions that yield the active streptokinase having native conformation. The maximum specific activity of the purified streptokinase was achieved by these methods. The refolded recombinant streptokinase was analyzed by RP-HPLC showing a purity of 99%. Size exclusion chromatography profile shows that there are minimal aggregates in the active streptokinase protein and the percentage of renaturation is around 99%.     

In vitro activation of yeast pro-carboxypeptidase Y expressed as inclusion bodies in Escherichia coli

The genes encoding pro-carboxypeptidase Ys (pro-CPYs) from Saccharomyces cerevisiae and Hansenula polymorpha were cloned and expressed in Escherichia coli. Most of the expressed pro-CPY was present in the form of inclusion bodies, accounting for about 35% of the total cellular protein. The inclusion bodies solubilized in 6 M guanidinum chloride were renatured by dilution 1:60 into renaturation buffer. Further refolding and activation were followed by the addition of 60 g ml_–1 proteinase K into the diluted solution. The specific activities of in vitro activated S. cerevisiae and H. polymorpha CPYs were found to be similar, representing about 25% of that of native S. cerevisiae CPY.     

Effects of l-arginine on refolding of lysine-tagged human insulin-like growth factor 1 expressed in Escherichia coli

Insulin-like growth factor 1 (IGF1), a therapeutic protein, is highly homologous to proinsulin in 3-dimensional structure. To highly express IGF1 in recombinant Escherichia coli, IGF1 was engineered to be fused with the 6-lysine tag and ubiquitin at its N-terminus (K6Ub-IGF1). Fed-batch fermentation of E. coli TG1/pAPT-K6Ub-IGF1 resulted in 60.8 g/L of dry cell mass, 18% of which was inclusion bodies composed of K6Ub-IGF1. Subsequent refolding processes were conducted using accumulated inclusion bodies. An environment of 50 mM bicine buffer (pH 8.5), 125 mM L-arginine, and 4 °C was chosen to optimize the refolding of K6Ub-IGF1, and 240 mg/L of denatured K6Ub-IGF1 was refolded with a 32% yield. The positive effect of L-arginine on K6Ub-IGF1 refolding might be ascribed to preventing unfolded K6Ub-IGF1 from undergoing self-aggregation and thus increasing its solubility. The simple dilution refolding, followed by cleavage of the fusion protein by site-specific UBP1 and chromatographic purification of IGF1, led production of authentic IGF1 with 97% purity and an 8.5% purification yield, starting from 500 mg of inclusion bodies composed of K6Ub-IGF1, as verified by various analytical tools, such as RP-HPLC, CD spectroscopy, MALDI-TOF mass spectrometry, and Western blotting. Thus, it was confirmed that L-arginine with an aggregation-protecting ability could be applied to the development of refolding processes for other inclusion body-derived proteins.     

A simplified bioprocess for human alpha-fetoprotein production from inclusion bodies

A simple and effective Escherichia coli (E. coli) bioprocess is demonstrated for the preparation of recombinant human alpha-fetoprotein (rhAFP), a pharmaceutically promising protein that has important immunomodulatory functions. The new rhAFP process employs only unit operations that are easy to scale and validate, and reduces the complexity embedded in existing inclusion body processing methods. A key requirement in the establishment of this process was the attainment of high purity rhAFP prior to protein refolding because (i) rhAFP binds easily to hydrophobic contaminants once refolded, and (ii) rhAFP aggregates during renaturation, in a contaminant- dependent way. In this work, direct protein extraction from cell suspension was coupled with a DNA precipitation-centrifugation step prior to purification using two simple chromatographic steps. Refolding was conducted using a single-step, redox-optimized dilution refolding protocol, with refolding success determined by reversed phase HPLC analysis, ELISA, and circular dichroism spectroscopy. Quantitation of DNA and protein contaminant loads after each unit operation showed that contaminant levels were reduced to levels comparable to traditional flowsheets. Protein microchemical modification due to carbamylation in this urea-based process was identified and minimized, yielding a final refolded and purified product that was significantly purified from carbamylated variants. Importantly, this work conclusively demonstrates, for the first time, that a chemical extraction process can substitute the more complex traditional inclusion body processing flowsheet, without compromising product purity and yield. This highly intensified and simplified process is expected to be of general utility for the preparation of other therapeutic candidates expressed as inclusion bodies.     

重组羧肽酶原B的复性方法研究

构建的羧肽酶原B表达质粒在大肠杆菌中获得高表达。但目的蛋白是以包涵体的形式存在。为了获得活性羧肽酶B,必须对其包涵体进行变复性。首先利用稀释复性确定了羧肽酶原B复性的最佳缓冲液;在凝胶过滤复性中,研究了柱长和洗脱流速对羧肽酶原B复性效率的影响;另外对比了稀释复性、透析复性、凝胶层析复性和Ni2 亲合层析法等四种方法对羧肽酶原B的复性效果。结果发现,这4种方法的复性效果有以下顺序:凝胶过滤复性>稀释复性>Ni2 亲合层析>透析复性。     

Refolding,purification and characterization of an organic solvent-tolerant lipase from Serratia marcescens ECU1010

Expression of recombinant proteins as inclusion bodies in bacteria is one of the most efficient ways to produce cloned proteins, as long as the inclusion bodies can be successfully refolded. In this study, the different parameters were investigated and optimized on the refolding of denatured lipase. The maximum lipase activity of 5000 U/L was obtained after incubation of denatured enzyme in a refolding buffer containing 20 mM Tris–HCl (pH 7.0), 1 mM Ca²⁺ at 20 °C. Then, the refolded lipase was purified to homogeneity by anion exchange chromatography. The purified refolded lipase was stable in broad ranges of temperatures and pH values, as well as in a series of water-miscible organic solvents. In addition, some water-immiscible organic solvents, such as petroleum ether and isopropyl ether, could reduce the polarity and increase the nonpolarity of the refolding system. The results of Fourier transform infrared (FT-IR) microspectroscopy were the first to confirm that lipase refolding could be further improved in the presence of organic solvents. The purified refolded lipase could enantioselectively hydrolyze trans-3-(4-methoxyphenyl) glycidic acid methyl ester [(±)-MPGM]. These features render the lipase attraction for biotechnological applications in the field of organic synthesis and pharmaceutical industry.     

Purification and characterization of recombinant sTRAIL expressed in Escherichia coli

As a potential anti-tumor protein, tumor necrosis factor-related apoptosis-inducing ligand(TRAIL) has drawn considerable attention. This report presented the purification and characterization ofsoluble TRAIL, expressed as inclusion bodies in E. coli. sTRAIL inclusion bodies were solubilized andrefolded at a high concentration up to 0.9 g/L by a simple dilution method. Refolded protein was purifiedto electrophoretic homogeneity by a single-step immobilized metal affinity chromatography. The purifiedsTRAIL had a strong cytotoxic activity against human pancreatic tumor cell line 1990, with EDs0 about 1.5mg/L. Circular dichroism and fluorescence spectrum analysis showed that the refolded sTRAIL had astructure similar to that of native protein with 13-sheet secondary structure. This efficient procedure ofsTRAIL renaturation may be useful for the mass production of this therapeutically important protein.     

Purification and refolding of a novel cancer/testis antigen BJ-HCC-2 expressed in the inclusion bodies of Escherichia coli

BJ-HCC-2 is one of the cancer/testis antigens that may be the most promising targets for tumor immunotherapy. To investigate the expression of BJ-HCC-2 protein in tumor cells and its capacity to elicit CTL response, the recombinant protein of BJ-HCC-2 was expressed in the inclusion bodies in Escherichia coli. The inclusion bodies were solubilized effectively with 0.3% N-lauroyl sarcosine in alkaline buffer. Under this denatured form, the BJ-HCC-2 protein carrying 6x histidine tag was purified with Ni-NTA affinity chromatography in a single step with a purity of over 97%. The yield of the purified protein was about 78%. The purified recombinant protein was refolded in a simple way. The correct refolding of the recombinant protein was verified in the recovery of its secondary and tertiary structures as assessed by circular dichroism and fluorescence emission spectra. The recovery rate of refolded protein was 92.1%. The renatured protein displayed its immunoreactivity with the antibodies to BJ-HCC-2 protein by Western blotting. This method of protein purification and refolding is easy to manipulate and may be applicable to the hydrophobic proteins that are unable to be purified by other methods.     

Expression, purification, and refolding of a novel immunotoxin containing humanized single-chain fragment variable antibody against CTLA4 and the N-terminal fragment of human perforin

Immunotoxins might be potential in treatment of cancer for their ability to kill selected cell populations. We constructed a novel immunotoxin hS83P34 by fusing N-terminal 34 amino acid fragment of human perforin to the C-terminus of humanized single-chain fragment variable antibody against CTLA4. The fusion protein was inductively expressed as inclusion bodies at a high level about 30% of total bacterial proteins. After washing with buffer containing 2 M urea, the purity of inclusion body was about 71%. The washed inclusion bodies were solubilized in 8 M urea and further purified to homogeneity (approximately 92% purity) by cation-exchange chromatography and Ni-agarose affinity chromatography under denaturing condition. The inclusion body refolding conditions were optimized following Pro-Matrix Protein Refolding Guide. After refolded in Tris buffer (pH 8.0) containing 1M urea, 0.8 M l-arginine, and 2 mM GSH:0.2 mM GSSG or 2 mM GSH:0.4 mM GSSG for 18h at 4 degrees C, over 90% proteins were recovered from inclusion bodies. In vitro dose-dependent cytotoxicity assay demonstrates that hS83P34 is only toxic to CTLA4-positive cells. IC(50) of hS83P34 for leukemic cells Raji and 6T-CEM are about 0.85 and 1.3 microM individually. Whereas, CTLA4-negative endothelial cell ECV-304 is resistant to hS83P34.     

Production and purification of refolded recombinant human IL-7 from inclusion bodies

A recombinant form of human rhIL-7 was overexpressed in Escherichia coli HMS174 (DE3) pLysS under the control of a T7 promoter. The resulting insoluble inclusion bodies were separated from cellular debris by cross-flow filtration and solubilized by homogenization with 6 M guanidine HCl. Attempts at refolding rhIL-7 from solubilized inclusion bodies without prior purification of monomeric, denatured rhIL-7 were not successful. Denatured, monomeric rhIL-7 was therefore initially purified by size-exclusion chromatography using Prep-Grade Pharmacia Superdex 200. Correctly folded rhIL-7 monomer was generated by statically refolding the denatured protein at a final protein concentration of 80-100 microg/ml in 100 mM Tris, 2mM EDTA, 500 mM L-arginine, pH 9.0, buffer with 0.55 g/l oxidized glutathione at 2-8 degrees C for at least 48 h. The refolded rhIL-7 was subsequently purified by low-pressure liquid chromatography, using a combination of hydrophobic interaction, cation-exchange, and size-exclusion chromatography. The purified final product was >95% pure by SDS-PAGE stained with Coomassie brilliant blue, high-pressure size-exclusion chromatography (SEC-HPLC), and reverse-phase HPLC. The endotoxin level was <0.05 EU/mg. The final purified product was biologically active in a validated IL-7 dependent pre-B-cell bioassay. In anticipation of human clinical trials, this material is currently being evaluated for safety and efficacy in non-human primate toxicology studies.     

Renaturation and activation of calf prochymosin produced in an insoluble form in Escherichia coli

Calf prochymosin produced in Escherichia coli cells harboring the expression plasmids was insoluble and formed large inclusion bodies, which were solubilized by 8 M urea. The conditions allowing correct refolding of denatured prochymosin were investigated. Dialysis at pH 10 in the presence of 500 mM NaCl was found to give the maximum renaturation, and subsequent acidic treatment for autocatalytic processing of refolded prochymosin allowed almost 100% recovery of chymosin.     

Renaturation of Escherichia coli-derived recombinant human macrophage colony-stimulating factor.

Recombinant human macrophage colony-stimulating factor (rhM-CSF), a homodimeric, disulfide bonded protein, was expressed in Escherichia coli in the form of inclusion bodies. Reduced and denatured rhM-CSF monomers were refolded in the presence of a thiol mixture (reduced and oxidized glutathione) and a low concentration of denaturing agent (urea or guanidinium chloride). Refolding was monitored by nonreducing gel electrophoresis and recovery of bioactivity. The effects of denaturant type and concentration, protein concentration, concentration of thiol/disulfide reagents, temperature, and presence of impurities on the kinetics of rhM-CSF renaturation were investigated. Low denaturant concentrations (<0.5 M urea) and high protein concentrations (>0.4 mg/ml) in the refolding mixture resulted in increased formation of aggregates, although aggregation was never significant even when refolding was carried out at room temperature. Higher protein concentration resulted in higher rates but did not lead to increased yields, due to the formation of unwanted aggregates. Experiments conducted at room temperature resulted in slightly higher rates than those conducted at 4 degrees C. Although the initial renaturation rate for solubilized inclusion body protein without purification was higher than that of the reversed-phase purified reduced denatured rhM-CSF, the final renaturation yield was much higher for the purified material. A maximum refolding yield of 95% was obtained for the purified material at the following refolding conditions: 0.5 M urea, 50 mM Tris, 1.25 mM DTT, 2 mM GSH, 2 mM GSSG, 22 degrees C, pH 8, [protein] = 0.13 mg/ml.     

Production of recombinant human serum albumin from Saccharomyces cerevisiae

Human serum albumin has been constitutively expressed in a Saccharomyces cerevisiae brewing yeast. After cell growth and disruption the product was associated with the insoluble fraction and represented approximately 1% of total cell protein. After the cell debris was extensively washed, the albumin was solubilized with 8 M urea and 28 mM 2-mercaptoethanol in 50 mM sodium carbonate buffer, pH 10. The denatured albumin was refolded by dialysis and further purified by anion exchange and gel filtration chromatography. Losses of renatured material could be reduced, or higher protein concentrations used during refolding, if the denatured product was purified by cation-exchange chromatography in urea prior to refolding. Apart from an additional N-terminal N-acetyl methionine, the refolded product proved identical to human serum albumin derived from plasma when compared by a variety of physical, chemical, and biological analytical methods.     

An efficient refolding method for the preparation of recombinant human prethrombin-2 and characterization of the recombinant-derived alpha-thrombin

Human recombinant prethrombin-2 was produced in Escherichia coli. The expressed prethrombin-2 formed intracellular inclusion bodies from which the protein was refolded by a simple one-step dilution process in buffer consisting of 50 mM Tris-HCl, containing 20 mM CaCl(2), 500 mM NaCl, 1 mM EDTA, 600 mM arginine, 1 mM cysteine, 0.1 mM cystine, 10% (v/v) glycerol, and 0.2% (w/v) Brij-58 at pH 8.5. After refolding, prethrombin-2 was purified by hirudin-based COOH-terminal peptide affinity chromatography, and then activated with Echis carinatus snake venom prothrombin activator (ecarin). The activated protein, alpha-thrombin, was then tested for several activities including activity toward chromogenic substrate, release of fibrinopeptide A from fibrinogen, activation of protein C, and thrombin-activatable fibrinolysis inhibitor, reactivity with antithrombin, clotting activity, and platelet aggregation. The kinetic data showed no differences in activity between our recombinant alpha-thrombin and plasma-derived alpha-thrombin. The yield of refolded recombinant human prethrombin-2 was about 4-7% of the starting amount of solubilized protein. In addition, the final yield of purified refolded protein was 0.5-1%, and about 1 mg of recombinant prethrombin-2 could be isolated from 1 liter of E. coli cell culture.