Highly efficient production of soluble proteins from insoluble inclusion bodies by a two-step-denaturing and refolding method

The production of recombinant proteins in a large scale is important for protein functional and structural studies, particularly by using Escherichia coli over-expression systems; however, approximate 70% of recombinant proteins are over-expressed as insoluble inclusion bodies. Here we presented an efficient method for generating soluble proteins from inclusion bodies by using two steps of denaturation and one step of refolding. We first demonstrated the advantages of this method over a conventional procedure with one denaturation step and one refolding step using three proteins with different folding properties. The refolded proteins were found to be active using in vitro tests and a bioassay. We then tested the general applicability of this method by analyzing 88 proteins from human and other organisms, all of which were expressed as inclusion bodies. We found that about 76% of these proteins were refolded with an average of >75% yield of soluble proteins. This "two-step-denaturing and refolding" (2DR) method is simple, highly efficient and generally applicable; it can be utilized to obtain active recombinant proteins for both basic research and industrial purposes.     

Single pH buffer refolding screen for protein from inclusion bodies

We previously reported the set up of an automated test for screening the refolding of recombinant proteins expressed as inclusion bodies in Escherichia coli[1]. The screen used 96 refolding buffers and was validated with 24 proteins, 70% of which remained soluble in at least one buffer. In the present paper, we have analyzed in more detail these experimental data to see if the refolding process can be driven by general rules. Notably, we found that proteins with an acidic isoelectric point (pI) refolded in buffers the average pH of which was alkaline and conversely. In addition, the number of refolding buffers wherein a protein remained soluble increased with the difference between its pI and the average pH of the buffers in which it refolded. A trend analysis of the other variables (ionic strength, detergents, etc.) was also performed. On the basis of this analysis, we devised and validated a new refolding screen made of a single buffer for acidic proteins and a single buffer for alkaline proteins.     

Review: Protein refolding and inactivation during bioseparation: Bioprocessing implications

The recombinant production of proteins leads to inclusion bodies which contain aggregated proteins in active, partially active, and inactive conformational states. These aggregated proteins must be extracted from the inclusion bodies, unfolded, and carefully refolded to the active and the stable conformational state. Mechanistic models for protein refolding are briefly presented. Different strategies and protocols are presented that lead to the active and stable protein conformational state. The techniques presented include chaperonin-assisted refolding, amino acid substitution, polyethylene glycolassisted refolding, protein refolding in reverse micelles, and antibody-assisted refolding of proteins. The techniques presented together provide a reasonable framework of the state-of-the-art and may be carefully applied to the bioseparation of other proteins and biological macromolecules of interest. (c) 1995 John Wiley & Sons, Inc.     

Penicillin-binding protein 2a of Streptococcus pneumoniae: expression in Escherichia coli and purification and refolding of inclusion bodies into a soluble and enzymatically active enzyme.

Penicillin-binding proteins (PBPs), targets of beta-lactam antibiotics, are membrane-bound enzymes essential for the biosynthesis of the bacterial cell wall. PBPs possess transpeptidase and transglycosylase activities responsible for the final steps of the bacterial cell wall cross-linking and polymerization, respectively. To facilitate our structural studies of PBPs, we constructed a 5'-truncated version (lacking bp from 1 to 231 encoding the N-terminal part of the protein including the transmembrane domain) of the pbp2a gene of Streptococcus pneumoniae and expressed the truncated gene product as a GST fusion protein in Escherichia coli. This GST fusion form of PBP2a, designated GST-PBP2a*, was expressed almost exclusively as inclusion bodies. Using a combination of high- and low-speed centrifugation, large amounts of purified inclusion bodies were obtained. These purified inclusion bodies were refolded into a soluble and enzymatically active enzyme using a single-step refolding method consisting of solubilization of the inclusion bodies with urea and direct dialysis of the solubilized preparations. Using these purification and refolding methods, approximately 37 mg of soluble GST-PBP2a* protein was obtained from 1 liter of culture. The identity of this refolded PBP2a* protein was confirmed by N-terminal sequencing. The refolded PBP2a*, with or without the GST-tag, was found to bind to BOCILLIN FL, a beta-lactam, and to hydrolyze S2d, an analog of the bacterial cell wall stem peptides. The S2d hydrolysis activity of PBP2a* was inhibited by penicillin G. In conclusion, using this expression system, and the purification and refolding methods, large amounts of the soluble GST-PBP2a* protein were obtained and shown to be enzymatically active.     

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.     

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.     

Matrix-assisted refolding of oligomeric small heat-shock protein Hsp26

Recombinant gene expression in the prokaryotic host Escherichia coli is of general interest for both biotechnology and basic research. Use of E. coli is inexpensive and advantageous due to the fully developed genetic accessibility. However, often insoluble target protein (inclusion body) accumulates in the cell. Especially when producing eukaryotic or disulfide bridged proteins in E. coli, inclusion body formation is observed. Nonetheless, insoluble protein can be regained and refolded in vitro. Commonly, renaturation of proteins is accomplished by methods involving dilution and/or dialysis. An interesting alternative is matrix-assisted refolding in which the denatured protein is refolded in the immobilized state. Here, matrix-assisted refolding was applied to refold a double cysteine variant of Hsp26, a small heat-shock protein from Saccharomyces cerevisiae which was insoluble after biosynthesis in E. coli BL21 (DE3) cells. This oligomeric protein was efficiently recovered from the insoluble fraction and refolded to its native oligomeric and chaperone-active state using ion exchange and size exclusion chromatography.     

A method for increasing the yield of properly folded recombinant fusion proteins: single-chain immunotoxins from renaturation of bacterial inclusion bodies.

Many proteins produced in Escherichia coli accumulate in inclusion bodies. We have systematically evaluated the parameters that affect the refolding and renaturation of enzymatically active molecules from bacterial inclusion bodies containing a recombinant single-chain immunotoxin, B3(Fv)-PE38KDEL. This recombinant molecule is composed of the variable domains of monoclonal antibody B3 (B3(Fv)) fused to a truncated mutant form of Pseudomonas exotoxin A (PE38KDEL). This immunotoxin kills carcinoma cells in vitro, causes tumor regression in animal tumor models, and is being developed as an anti-cancer therapeutic agent (Brinkmann et al., 1991, Proc. Natl. Acad. Sci. USA 88, 8616-8620). Like many other recombinant proteins, B3(Fv)-PE38KDEL is produced in E. coli in inclusion bodies and must be denatured and refolded to become active. This requires correct folding, formation of native disulfide bonds, and the association of different domains. All these steps are strongly dependent on the renaturation conditions used. Optimum conditions of refolding were obtained by the addition of reduced and oxidized thiol reagents to promote disulfide bond formation and the addition of a labilizing agent such as L-arginine. Furthermore, the necessity to reactivate proteins at low protein concentrations due to its tendency to aggregate at high concentrations was overcome by a step-by-step addition of denatured and reduced protein into the refolding solution. This approach should be useful for the production of active forms of other recombinant proteins.     

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.     

Preparative protein refolding

The rapid provision of purified native protein underpins both structural biology and the development of new biopharmaceuticals. The dominance of Escherichia coli as a cellular biofactory depends on technology for solubilizing and refolding proteins that are expressed as insoluble inclusion bodies. Such technology must be scale invariant, easily automated, generic for a broad range of similar proteins and economical. Refolding methods relying on denaturant dilution and column-based approaches meet these criteria. Recent developments, particularly in column-based methods, promise to extend the range of proteins that can be refolded successfully. Developments in preparing denatured purified protein and in the analysis of protein refolding products promise to remove bottlenecks in the overall process. Combined, these developments promise to facilitate the rapid and automated determination of appropriate refolding conditions and to simplify scale-up.     

重组人MASP2蛋白在大肠杆菌中的表达和纯化

目的:获得酶原形式的重组人甘露聚糖结合凝集素相关丝氨酸蛋白酶2(MASP2)。方法:在大肠杆菌中诱导表达重组人MASP2全长蛋白,包涵体裂解后,经复性、透析、浓缩、考马斯亮蓝染色、SDS-PAGE及Western印迹,鉴定纯化结果及酶活性。结果:复性后的MASP2蛋白经考马斯亮蓝染色未见杂带。自激活实验表明,当MASP2浓度在1μmool/L以下时,无论在4℃还是37℃,都能较稳定地保持酶原形式;蛋白浓度为3.5μmool/L时只能在4℃保持稳定,37℃发生自激活;蛋白浓度达到12μmool/L后,在4℃时已不能稳定存在。结论:获得了较纯的重组人MASP2蛋白,且具有自激活活性。     

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.     

In vitro folding of alpha-helical membrane proteins

For large-scale production, as required in structural biology, membrane proteins can be expressed in an insoluble form as inclusion bodies and be refolded in vitro. This requires refolding conditions where the native form is thermodynamically stable and where nonproductive pathways leading to aggregation are avoided. Examples of successful refolding are reviewed and general guidelines to establish refolding protocols of membrane proteins are presented.     

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.     

In vitro folding of alpha-helical membrane proteins

For large-scale production, as required in structural biology, membrane proteins can be expressed in an insoluble form as inclusion bodies and be refolded in vitro. This requires refolding conditions where the native form is thermodynamically stable and where nonproductive pathways leading to aggregation are avoided. Examples of successful refolding are reviewed and general guidelines to establish refolding protocols of membrane proteins are presented.     

High recovery refolding of rhG-CSF from Escherichia coli, using urea gradient size exclusion chromatography

Protein folding liquid chromatography (PFLC) is a powerful tool for simultaneous refolding and purification of recombinant proteins in inclusion bodies. Urea gradient size exclusion chromatography (SEC) is a recently developed protein refolding method based on the SEC refolding principle. In the presented work, recombinant human granulocyte colony-stimulating factor (rhG-CSF) expressed in Escheriachia coli (E. coli) in the form of inclusion bodies was refolded with high yields by this method. Denatured/reduced rhG-CSF in 8.0 mol.L(-1) urea was directly injected into a Superdex 75 column, and with the running of the linear urea concentration program, urea concentration in the mobile phase and around the denatured rhG-CSF molecules was decreased linearly, and the denatured rhG-CSF was gradually refolded into its native state. Aggregates were greatly suppressed and rhG-CSF was also partially purified during the refolding process. Effects of the length and the final urea concentration of the urea gradient on the refolding yield of rhG-CSF by using urea gradient SEC were investigated respectively. Compared with dilution refolding and normal SEC with a fixed urea concentration in the mobile phase, urea gradient SEC was more efficient for rhG-CSF refolding--in terms of specific bioactivity and mass recovery, the denatured rhG-CSF could be refolded at a larger loading volume, and the aggregates could be suppressed more efficiently. When 500 microL of solubilized and denatured rhG-CSF in 8.0 mol.L(-1) urea solution with a total protein concentration of 2.3 mg.mL(-1) was loaded onto the SEC column, rhG-CSF with a specific bioactivity of 1.0 x 10(8) IU.mg(-1) was obtained, and the mass recovery was 46.1%.     

Refolding process of cysteine-rich proteins:Chitinase as a model

Background:

Recombinant proteins overexpressed in E. coli are usually deposited in inclusion bodies. Cysteines in the protein contribute to this process. Inter- and intra- molecular disulfide bonds in chitinase, a cysteine-rich protein, cause aggregation when the recombinant protein is overexpressed in E. coli. Hence, aggregated proteins should be solubilized and allowed to refold to obtain native- or correctly- folded recombinant proteins.

Methods:

Dilution method that allows refolding of recombinant proteins, especially at high protein concentrations, is to slowly add the soluble protein to refolding buffer. For this purpose: first, the inclusion bodies containing insoluble proteins were purified; second, the aggregated proteins were solubilized; finally, the soluble proteins were refolded using glutathione redox system, guanidinium chloride, dithiothreitol, sucrose, and glycerol, simultaneously.

Results:

After protein solubilization and refolding, SDS-PAGE showed a 32 kDa band that was recognized by an anti-chitin antibody on western blots.

Conclusions:

By this method, cysteine-rich proteins from E. coli inclusion bodies can be solubilized and correctly folded into active proteins.Key Words: Chitinase, Cysteine-rich proteins, Protein refolding, Protein solubilization     

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.     

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.     

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.