Refolding of recombinant human interferon ��-2a from Escherichia coli by urea gradient size exclusion chromatography

Protein refolding is still a puzzle in the production of recombinant proteins expressed as inclusion bodies (IBs) in Escherichia coli. Gradient size exclusion chromatography (SEC) is a recently developed method for refolding of recombinant proteins in IBs. In this study, we used a decreasing urea gradient SEC for the refolding of recombinant human interferon ??-2a (rhIFN??-2a) which was overexpressed as IBs in E. coli. In chromatographic process, the denatured rhIFN??-2a would pass along the 8.0?C3.0 M urea gradient and refold gradually. Several operating conditions, such as final concentration of urea along the column, gradient length, the ratio of reduced to oxidized glutathione and flow rate were investigated, respectively. Under the optimum conditions, 1.2 × 10⁸ IU/mg of specific activity and 82% mass recovery were obtained from the loaded 10 ml of 1.75 mg/ml denatured protein, and rhIFN??-2a was also purified during this process with the purity of higher than 92%. Compared with dilution method, urea gradient SEC was more efficient for the rhIFN??-2a refolding in terms of specific activity and mass recovery.     

A Comparative Investigation on Different Refolding Strategies of Recombinant Human Tissue-type Plasminogen Activator Derivative

Recombinant human tissue-type plasminogen activator derivative (r-PA), fused with thioredoxin (Trx), was expressed in Escherichia coli. The resultant fusion protein, Trx-r-PA, was almost completely in the form of inclusion bodies and without activity. Different refolding strategies were investigated including different post-treatment of solubilized Trx-r-PA inclusion bodies, on-column refolding by size-exclusion chromatography (SEC) using three gel types (Sephacryl S-200, S-300 and S-400), refolding by Sephacryl S-200 with a urea gradient and two-stage temperature control in refolding. An optimized on-column refolding process for Trx-r-PA inclusion bodies was established. The collected Trx-r-PA inclusion bodies were dissolved in 6 m guanidine hydrochloride (Gdm·HCl), and the denatured protein was separated from dithiothreitol (DTT) and Gdm·HCl with a G25 column and simultaneously dissolved in 8 m urea containing oxidized glutathione (GSSG). Finally a refolding of Trx-r-PA protein on Sephacryl S-200 column with a decreasing urea gradient combined with two-stage temperature control was employed, and the activity recovery of refolded protein was increased from 3.6 to 13.8% in comparison with the usual dilution refolding. Revisions requested 31 October 2005; Revisions received 20 December 2005     

On-column refolding of recombinant human interferon-gamma inclusion bodies by expanded bed adsorption chromatography

A refolding strategy was described for on-column refolding of recombinant human interferon-gamma (rhIFN-gamma) inclusion bodies by expanded bed adsorption (EBA) chromatography. After the denatured rhIFN-gamma protein bound onto the cation exchanger of STREAMLINE SP, the refolding process was performed in expanded bed by gradually decreasing the concentration of urea in the buffer and the refolded rhIFN-gamma protein was recovered by the elution in packed bed mode. It was demonstrated that the denatured rhIFN-gamma protein could be efficiently refolded by this method with high yield. Under appropriate experimental conditions, the protein yield and specific activity of rhIFN-gamma was up to 52.7% and 8.18 x 10(6) IU/mg, respectively.     

Cloning, expression, and refolding of a secretory protein ESAT-6 of Mycobacterium tuberculosis

A DNA encoding the 6-kDa early secretory antigenic target (ESAT-6) of Mycobacterium tuberculosis was inserted into a bacterial expression vector of pQE30 resulting in a 6x His-esat-6 fusion gene construction. This plasmid was transformed into Escherichia coli strain M15 and effectively expressed. The expressed fusion protein was found almost entirely in the insoluble form (inclusion bodies) in cell lysate. The inclusion bodies were solubilized with 8M urea or 6M guanidine-hydrochloride at pH 7.4, and the recombinant protein was purified by Ni-NTA column. The purified fusion protein was refolded by dialysis with a gradient of decreasing concentration of urea or guanidine hydrochloride or by the size exclusion protein refolding system. The yield of refolded protein obtained from urea dialysis was 20 times higher than that from guanidine-hydrochloride. Sixty-six percent of recombinant ESAT-6 was successfully refolded as monomer protein by urea gradient dialysis, while 69% of recombinant ESAT-6 was successfully refolded as monomer protein by using Sephadex G-200 size exclusion column. These results indicate that urea is more suitable than guanidine-hydrochloride in extracting and refolding the protein. Between the urea gradient dialysis and the size exclusion protein refolding system, the yield of the monomer protein was almost the same, but the size exclusion protein refolding system needs less time and reagents.     

Recombinant Human Ribosomal Protein S16: Expression,Purification, Refolding,and Structural Stability

The cDNA of human ribosomal protein S16 was cloned into the expression vector pET-15b. Large-scale production of the recombinant protein was carried out in E. coli cells and highly purified protein was isolated. A method for refolding the protein from inclusion bodies was optimized. The secondary structure content of the refolded protein was analyzed by CD spectroscopy. It was found that 21 +/- 4% of the amino acid sequence of the protein forms alpha-helices and 24 +/- 3% is in beta-strands. The protein structure stability was studied at various pH values and urea concentrations. The protein is quickly denatured at pH above 8.0, whereas increasing of urea concentration causes slow unfolding of the protein.     

A Combined Refolding Technique for Recombinant Human Interferon-γ Inclusion Bodies by Ion-exchange Chromatography with a Urea Gradient

Summary A refolding strategy was described for on-column refolding of recombinant human interferon-γ (rhIFN-γ) inclusion bodies by ion-exchange chromatography (IEC). The rhIFN-γ was expressed in E. colias inclusion bodies. Triton X-100 was used first to wash the rhIFN-γ inclusion bodies before chromatographic refolding. The refolding process was performed by gradually decreasing the concentration of urea in the column after the denatured rhIFN-γ protein had bound onto the ion-exchange gel SP-Sepharose Fast Flow. The refolding and purification process for the denatured rhIFN-γ was carried through simultaneously and the purity of the refolded rhIFN-γ was up to 95%. The effects of protein loading, flow rate, urea gradient length and final urea concentration on the refolding were investigated in detail. Under the optimum conditions, the specific activity of rhIFN-γ was up to 7.5 × 10⁵ IU mg⁻¹and active protein recovery was up to 54%.     

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.     

Chromatographic methods for the isolation of,and refolding of proteins from,Escherichia coli inclusion bodies

New methods for the chromatographic isolation of inclusion bodies directly from crude Escherichia coli homogenates and for the refolding of denatured protein are presented. The traditional method of differential centrifugation for the isolation of purified inclusion bodies is replaced by a single gel-filtration step. The principle is that the exclusion limit of the gel particles is chosen such that only the inclusion bodies are excluded, i.e., all other components of the crude homogenate penetrate the gel under the conditions selected. In the novel column refolding process, a decreasing gradient of denaturant (urea or Gu-HCl), combined with an increasing pH gradient, is introduced into a gel-filtration column packed with a gel medium that has an exclusion limit lower than the molecular mass of the protein to be refolded. A limited sample volume of the protein, dissolved in the highest denaturant concentration at the lowest pH of the selected gradient combination, is applied to the column. During the course of elution, the zone of denatured protein moves down the column at a speed approximately threefold higher than that of the denaturant. This means that the protein sample will gradually pass through areas of increasingly lower denaturant concentrations and higher pH, which promotes refolding into the native conformation. The shape and slope of the gradients, as well as the flow rate, will influence the refolding rate and can be adjusted for different protein samples. The principle is illustrated using a denatured recombinant scFv fusion protein obtained from E. coli inclusion bodies.     

High productivity refolding of an inclusion body protein using pulsed-fed size exclusion chromatography

Protein refolding using size exclusion chromatography (SEC) is advantageous over conventional refolding methods in terms of ease of automation, simultaneous purification capabilities, and the non-adsorptive protein–matrix interaction which eliminates steric constraints. Despite these advantages, the widespread use of SEC refolding remains restricted by low process productivity and product concentration bottlenecks. This study aims to address those limitations and exploit SEC advantages for large-scale refolding applications. Specifically, this study reports the development of a pulsed-fed size exclusion chromatography (PF-SEC) refolding platform, which successfully refolded E. coli-derived α-fetoprotein (AFP) to achieve 53% refolding yield at 0.9 mg/ml AFP refolding concentration. AFP was introduced into the column by pulsed injection to increase feed load, while suppressing concentration-induced aggregation. Refolding was initiated by a urea gradient in the column, where the gradient length could be readily adjusted to complement pulsed feeding patterns. AFP refolding productivity with PF-SEC improved by 8- and 64-fold compared to ion-exchange chromatography refolding and pulsed dilution refolding, respectively, at a fixed refolding concentration. Through a unique integration of pulsed feeding and urea gradient development, this new PF-SEC refolding methodology overcomes ‘productivity and concentration’-related disadvantages inherent in SEC, and will be scalable for large-scale protein refolding applications.     

Effect of column dimensions and flow rates on size-exclusion refolding of beta-lactamase

We have investigated the effect of changing the column diameter and length on the size exclusion chromatography (SEC) refolding of beta-lactamase from Escherichia coli-derived inclusion bodies (IBs). Inclusion bodies were recovered and solubilised in 6 M GdnHCl and 5 mM DTT. Up to 16 mg of denatured, solubilised beta-lactamase was loaded onto size exclusion columns packed with Sephacryl S-300 media (fractionation range: 10(4)-1.5 x 10(6) Da). beta-Lactamase was refolded by eluting the loaded sample with 1 M urea in 0.05 M phosphate buffer, pH 7 at 23 degrees C. The following columns were studied: 26 x 400, 16 x 400 and 26 x 200 mm, with a range of mobile phase flow rates from 0.33 to 4.00 ml/min. beta-Lactamase was successfully refolded in all three columns and at all flow rates studied. The beta-lactamase activity peak coincided with the major protein peak. Reducing the column diameter had little effect on refolding performance. The enzyme activity recovered was relatively independent of the mobile phase linear velocity. Reducing the column length gave a poorer resolution of the protein peaks, but the enzyme activity peaks were well resolved. Calculation of the partition coefficients for beta-lactamase activity showed that the 26 x 400 column gave the greatest refolding performance.     

蛋白质的排阻色谱复性的新进展

外源蛋白在大肠杆菌中高效表达时 ,常常形成不溶的、无活性的包涵体 ,包涵体蛋白的复性是重组蛋白生产过程中的一个技术难题。排阻色谱 (sizeexclusionchromatography ,SEC)用于蛋白复性是一种较新的、适用于任何一种蛋白的方法 ,与常用的稀释复性法相比 ,它能在高的起始蛋白浓度下对蛋白进行复性 ,活性回收率较高 ,同时又能使目标蛋白得到一定程度的纯化。对使用SEC复性的进展进行了评述 ,其内容包括SEC复性的原理及其复性过程中的影响因素 ,并对其未来发展进行了展望。     

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.     

Soybean disease resistance protein RHG1-LRR domain expressed, purified and refolded from Escherichia coli inclusion bodies: preparation for a functional analysis

Introduction and expression of foreign genes in bacteria often results accumulation of the foreign protein(s) in inclusion bodies (IBs). The subsequent processes of refolding are slow, difficult and often fail to yield significant amounts of folded protein. RHG1 encoded by rhg1 was a soybean (Glycine max L. Merr.) transmembrane receptor-like kinase (EC 2.7.11.1) with an extracellular leucine-rich repeat domain. The LRR of RHG1 was believed to be involved in elicitor recognition and interaction with other plant proteins. The aim, here, was to express the LRR domain in Escherichia coli (RHG1-LRR) and produce refolded protein. Urea titration experiments showed that the IBs formed in E. coli by the extracellular domain of the RHG1 protein could be solubilized at different urea concentrations. The RHG1 proteins were eluted with 1.0-7.0M urea in 0.5M increments. Purified RHG1 protein obtained from the 1.5 and 7.0M elutions was analyzed for secondary structure through circular dichroism (CD) spectroscopy. Considerable secondary structure could be seen in the former, whereas the latter yielded CD curves characteristic of denatured proteins. Both elutions were subjected to refolding by slowly removing urea in the presence of arginine and reduced/oxidized glutathione. Detectable amounts of refolded protein could not be recovered from the 7.0M urea sample, whereas refolding from the 1.5M urea sample yielded 0.2mg/ml protein. The 7.0M treatment resulted in the formation of a homogenous denatured state with no apparent secondary structure. Refolding from this fully denatured state may confer kinetic and/or thermodynamic constraints on the refolding process, whereas the kinetic and/or thermodynamic barriers to attain the folded conformation appeared to be lesser, when refolding from a partially folded state.     

High-level Recombinant Expression and Refolding of Lysozyme from the Marine Shrimp <Emphasis Type="Italic">Marsupenaeus japonicus</Emphasis>

Shrimp lysozyme is as an antibacterial enzyme that participates in the innate defense against the invasion of bacterial pathogens. In this study, the lysozyme gene from hemocytes of the shrimp Marsupenaeus japonicus was isolated and characterized. The M. japonicus lysozyme (MjLys) encodes a polypeptide of 158 amino acids (aa) that includes an 18 aa signal peptide. The gene fragment encoding the mature MjLys protein was subcloned into the expression vector pET-32a(+) and transformed into E. coli BL21(DE3)pLysS, and the protein was strongly expressed in insoluble inclusion bodies. Following extraction using urea, the denatured recombinant protein was refolded by on-column Ni²⁺ affinity chromatography or dialysis with a gradient of decreasing urea concentration. Approximately 50% of the recombinant MjLys was successfully refolded into monomeric protein using urea gradient dialysis, while 30% was salvaged using on-column refolding. Purified MjLys exhibited significant antibacterial activity against Gram-positive bacteria Micrococcus lysodeikticus and Staphylococcus aureus. This efficient over-expression and refolding method can provide the large quantities of biologically active protein required for further biochemical and structural studies and potential biotechnological applications.     

Refolding and purification of recombinant human interferon-γ expressed as inclusion bodies inEscherichia coli using size exclusion chromatography

A size exclusion chromatography (SEC) process, in the presence of denaturant in the refolding buffer was developed to refold recombinant human interferon-γ (rhIFN-γ) at a high concentration. The rhIFN-γ was overexpressed inE. coli, resulting in the formation of inactive inclusion bodies (IBs). The IBs were first solubilized in 8 M urea as the denaturant, and then the refolding process performed by decreasing the urea concentration on the SEC column to suppress protein aggregation. The effects of the urea concentration, protein loading mode and column height during the refolding step were investigated. The combination of the bufferexchange effect of SEC and a moderate urea concentration in the refolding buffer resulted in an efficient route for producing correctly folded rhIFN-γ, with protein recovery of 67.1% and specific activity up to 1.2×10⁷ IU/mg.     

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.     

Refolding and purification of recombinant human granulocyte colony-stimulating factor using hydrophobic interaction chromatography at a large scale

High level expression of recombinant human granulocyte colony-stimulating factor (rhG-CSF) in Escherichia coli (E. coli) usually forms insoluble and inactive aggregates, i.e. inclusion bodies. In the present work, high performance hydrophobic interaction chromatography (HPHIC) was applied to the refolding of rhG-CSF, which was solubilized by 8.0 mol L^?1 urea from the inclusion bodies. First a laboratorial scale column (10 mm × 20 mm I.D.) was employed to study the refolding process. Several factors, including concentration of ammonium sulfate, pH of the mobile phase and flow rate, were investigated in details. The results indicated that the rhG-CSF produced by E. coli could be successfully refolded with simultaneous purification by using HPHIC. The refolding process was further scaled up by using a large column (50 mm × 200 mm I.D.). 200 mL of rhG-CSF solution solubilized by 8.0 mol L^?1 urea, with a total amount of protein around 1.6 g, could be loaded onto the large column at one time. Under these conditions, the obtained rhG-CSF had a specific activity of 2.3 × 10⁸ IU mg^?1 and a purity of 95.4%, the mass recovery during the purification was 36.9%. This work might have great impact on practical production of rhG-CSF, and it also shed a light on protein refolding using liquid chromatography at large scales.     

Intensified process for the purification of an enzyme from inclusion bodies using integrated expanded bed adsorption and refolding

This work describes the integration of expanded bed adsorption (EBA) and adsorptive protein refolding operations in an intensified process used to recover purified and biologically active proteins from inclusion bodies expressed in E. coli. Delta(5)-3-Ketosteroid isomerase with a C-terminal hexahistidine tag was expressed as inclusion bodies in the cytoplasm of E. coli. Chemical extraction was used to disrupt the host cells and simultaneously solubilize the inclusion bodies, after which EBA utilizing immobilized metal affinity interactions was used to purify the polyhistidine-tagged protein. Adsorptive refolding was then initiated in the column by changing the denaturant concentration in the feed stream from 8 to 0 M urea. Three strategies were tested for performing the refolding step in the EBA column: (i) the denaturant was removed using a step change in feed-buffer composition, (ii) the denaturant was gradually removed using a gradient change in feed-buffer composition, and (iii) the liquid flow direction through the column was reversed and adsorptive refolding performed in the packed bed. Buoyancy-induced mixing disrupted the operation of the expanded bed when adsorptive refolding was performed using either a step change or a rapid gradient change in feed-buffer composition. A shallow gradient reduction in denaturant concentration of the feed stream over 30 min maintained the stability of the expanded bed during adsorptive refolding. In a separate experiment, buoyancy-induced mixing was completely avoided by performing refolding in a settled bed, which achieved comparable yields to refolding in an expanded bed but required a slightly more complex process. A total of 10% of the available KSI-(His(6)) was recovered as biologically active and purified protein using the described purification and refolding process, and the yield was further increased to 19% by performing a second iteration of the on-column refolding operation. This process should be applicable for other polyhistidine tagged proteins and is likely to have the greatest benefit for proteins that tend to aggregate when refolded by dilution.     

Refolding and purification of yeast carboxypeptidase Y expressed as inclusion bodies in Escherichia coli

The genes encoding carboxypeptidase Y (CPY) and CPY propeptide (CPYPR) from Saccharomyces cerevisiae were cloned and expressed in Escherichia coli. Six consecutive histidine residues were fused to the C-terminus of the CPYPR for facilitated purification. High-level expression of CPY and CPYPR-His(6) was achieved but most of the expressed proteins were present in the form of inclusion bodies in the bacterial cytoplasm. The CPY and CPYPR-His(6) produced as inclusion bodies were separated from the cells and solubilized in 6 and 3 M guanidinium chloride, respectively. The denatured CPYPR-His(6) was refolded by dilution 1:30 into the renaturation buffer (50 mM Tris-HCl containing 0.5 M NaCl and 3 mM EDTA, pH 8.0), and the refolded CPYPR-His(6) was further purified to 90% purity by single-step immobilized metal ion affinity chromatography. The denatured CPY was refolded by dilution 1:60 into the renaturation buffer containing CPYPR-His(6) at various concentrations. Increasing the molar ratio of CPYPR-His(6) to CPY resulted in an increase in the CPY refolding yield, indicating that the CPYPR-His(6) plays a chaperone-like role in in vitro folding of CPY. The refolded CPY was purified to 92% purity by single-step p-aminobenzylsuccinic acid affinity chromatography. When refolding was carried out in the presence of 10 molar eq CPYPR-His(6), the specific activity, N-(2-furanacryloyl)-l-phenylalanyl-l-phenylalanine hydrolysis activity per milligram of protein, of purified recombinant CPY was found to be about 63% of that of native S. cerevisiae CPY.