Purification of the Caenorhabditis elegans transposase Tc1A refolded during gel filtration chromatography

Full-length recombinant transposase Tc1A from Caenorhabditis elegans (343 amino acids) expressed in Escherichia coli BL21 in inclusion bodies has been purified in a high yield in a soluble form. The procedure includes denaturation of the inclusion bodies followed by refolding of the Tc1A protein by gel filtration. This last step is absolutely crucial to give a high yield of soluble and active protein since it allows the physical separation of the aggregates from intermediates that give rise to correctly refolded protein. This step is very sensitive to the concentration of protein. Good yields of refolded protein are obtained by refolding 2 to 12 mg of denatured protein. The other purification steps involve the initial use of gel filtration under denaturing conditions and a final step of ion-exchange chromatography. Biological activity of the purified protein was confirmed in an in vitro transposon excision assay and its DNA-binding capacity by UV crosslinking. This new Tc1A purification procedure gives a yield of 12-16 mg/liter E. coli culture, in a form suitable for crystallization studies.     

Purification of truncated and mutated Chemotaxis Inhibitory Protein of Staphylococcus aureus--an anti-inflammatory protein

The Chemotaxis Inhibitory Protein of Staphylococcus aureus (CHIPS) binds and blocks the C5a receptor (C5aR) and formyl-peptide receptor (FPR). This way, CHIPS is a potent inhibitor of the immune cell recruitment associated with inflammation. Truncation of the protein and the introduction of mutations, shifts the expression towards the insoluble fraction of Escherichia coli, whereas the wild-type protein can be solubly expressed. A protocol for expression and tag independent purification of biologically active CHIPS variants has been established to enable further characterization of an improved CHIPS variant, called ADC-1004. The CHIPS variants were purified by washing of E. coli inclusion bodies followed by refolding and gel filtration. New techniques were utilized to optimize the purification process. Expression in inclusion bodies was increased by the use of Ultra Yield^™ flasks and optimal refolding conditions were determined by the use of the iFOLD Refolding System 2^™.The folding and biological activity of the purified proteins were analyzed by circular dichroism (CD) spectroscopy and flow cytometry, respectively, and compared to solubly produced CHIPS_31–113 and wild-type CHIPS_1–121. We show that the CHIPS variants produced in inclusion bodies can be refolded and purified to achieve equal biological activity as solubly produced CHIPS_31–113 and wild-type CHIPS_1–121. The truncation causes minor structural changes while purification from inclusion bodies or the soluble fraction does not further affect the structure.     

SOn-column Protein Refolding for Crystallization

One major bottleneck in protein production in Escherichia coli for structural genomics projects is the formation of insoluble protein aggregates (inclusion bodies). The efficient refolding of proteins from inclusion bodies is becoming an important tool that can provide soluble native proteins for structural and functional studies. Here we report an on-column refolding method established at the Berkeley Structural Genomics Center (BSGC). Our method is a combination of an ‘artificial chaperone-assisted refolding’ method previously proposed and affinity chromatography to take advantage of a chromatographic step: less time-consuming, no filtration or concentration, with the additional benefit of protein purification. It can be easily automated and formatted for high-throughput process.     

Optimized procedures for producing biologically active chemokines

We describe here two strategies to produce biologically active chemokines with authentic N-terminal amino acid residues. The first involves producing the target chemokine with an N-terminal 6×His-SUMO tag in Escherichia coli as inclusion bodies. The fusion protein is solubilized and purified with Ni–NTA–agarose in denaturing reagents. This is further followed by tag removal and refolding in a redox refolding buffer. The second approach involves expressing the target chemokine with an N-terminal 6×His-Trx-SUMO tag in an engineered E. coli strain that facilitates formation of disulfide bonds in the cytoplasm. Following purification of the fusion protein via Ni–NTA and tag removal, the target chemokine is refolded without redox buffer and purified by reverse phase chromatography. Using the procedures, we have produced more than 15 biologically active chemokines, with a yield of up to 15 mg/L.     

New Approaches for Functional Expression of Recombinant Horseradish Peroxidase C In Escherichia Coli

Horseradish peroxidase (HRP) is an important enzyme in bio- and immunochemical analysis. In a first approach we expressed HRP with a C-terminal histidine tag in the Escherichia coli (E. coli) periplasm. On the one hand this led to functionally active HRP-His at a low yield of 0.5mg/l of culture medium. On the other hand the affinity tag introduced allowed for optimization of the downstream processing of HRP-His refolded from inclusion bodies, thereby increasing the yield of homogeneous enzyme to 8-10mg/l of E. coli culture medium when expressed conventionally in E. coli cytosol as the second approach. The final refolding/reconstitution protocol includes crucial gel filtration steps to remove constituents of the refolding medium and, in particular, imidazole from the active site of HRP-His, resulting in spectral (Soret band maximum of 403 nm) and catalytic properties of the refolded HRP-His (1160U/mg with 2, 2′-Azino-bis[3-ethylbenzthiazoline-6-sulfonate] as substrate) indistinguishable from those of the plant-derived HRP.     

Mammalian G protein-coupled receptor expression in Escherichia coli: II. Refolding and biophysical characterization of mouse cannabinoid receptor 1 and human parathyroid hormone receptor 1

G protein-coupled receptors (GPCRs) represent approximately 3% of the human proteome. They are involved in a large number of diverse processes and, therefore, are the most prominent class of pharmacological targets. Besides rhodopsin, X-ray structures of classical GPCRs have only recently been resolved, including the β1 and β2 adrenergic receptors and the A2A adenosine receptor. This lag in obtaining GPCR structures is due to several tedious steps that are required before beginning the first crystallization experiments: protein expression, detergent solubilization, purification, and stabilization. With the aim to obtain active membrane receptors for functional and crystallization studies, we recently reported a screen of expression conditions for approximately 100 GPCRs in Escherichia coli, providing large amounts of inclusion bodies, a prerequisite for the subsequent refolding step. Here, we report a novel artificial chaperone-assisted refolding procedure adapted for the GPCR inclusion body refolding, followed by protein purification and characterization. The refolding of two selected targets, the mouse cannabinoid receptor 1 (muCB1R) and the human parathyroid hormone receptor 1 (huPTH1R), was achieved from solubilized receptors using detergent and cyclodextrin as protein folding assistants. We could demonstrate excellent affinity of both refolded and purified receptors for their respective ligands. In conclusion, this study suggests that the procedure described here can be widely used to refold GPCRs expressed as inclusion bodies in E. coli.     

Purification, Refolding of Hybrid hIFNγ-Kringle 5 Expressed in Escherichia coli

The DNA sequence coding for plasminogen kringle 5 (pK5), an inhibitor of angiogenesis, was fused with that coding for interferon gamma and over-produced in the form of inactive inclusion bodies in E. coli. The amount of fusion protein was about 40% of total protein produced. The fusion protein contained in the inclusion bodies was solubilized in 8 m urea and purified by anion-exchange chromatography. We employed the orthogonal experimental design L₁₆(4⁵) (5 factors, 4 levels, 16 experiments) procedure for researching the influence of denaturant, aggregation suppressor l-arginine, NaCl, pH, and glycine on the refolding procedure. Our results suggest that the presence of appropriate l-arginine, NaCl, and denaturant in the refolding buffer inhibits the aggregation of the fusion protein and increases the yield of renatured protein with biological activity. The refolded fusion protein, γIFN/pk5, has in vitro anti-endothelial cell proliferation activity. Received: 24 July 2000 / Accepted: 21 September 2000     

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.     

High throughput purification of recombinant human growth hormone using radial flow chromatography

Recombinant human growth hormone (r-hGH) was expressed in Escherichia coli as inclusion bodies. Using fed-batch fermentation process, around 670 mg/L of r-hGH was produced at a cell OD600 of 35. Cell lysis followed by detergent washing resulted in semi-purified inclusion bodies with more than 80% purity. Purified inclusion bodies were homogenous in preparation having an average size of 0.6 μm. Inclusion bodies were solubilized at pH 12 in presence of 2 M urea and refolded by pulsatile dilution. Refolded protein was purified with DEAE-anion exchange chromatography using both radial and axial flow column (50 ml bed volume each). Higher buffer flow rate (30 ml/min) in radial flow column helped in reducing the batch processing time for purification of refolded r-hGH. Radial column based purification resulted in high throughput recovery of diluted refolded r-hGH in comparison to axial column. More than 40% of inclusion body protein could be refolded into bioactive form using the above method in a single batch. Purified r-hGH was analyzed by mass spectroscopy and found to be bioactive by Nb2 cell line proliferation assay. Inclusion body enrichment, mild solubilization, pulsatile refolding and radial flow chromatography worked co-operatively to improve the overall recovery of bioactive protein from inclusion bodies.     

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%.     

Refolding and purification of recombinant human (Pro)renin receptor from Escherichia coli by ion exchange chromatography

Purification of the recombinant human renin receptor (rhRnR) is a major aspect of its biological or biophysical analysis, as well as structural research. A simple and efficient method for the refolding and purification of rhRnR expressed in Escherichia coli with weak anion‐exchange chromatography (WAX) was presented in this work. The solution containing denatured rhRnR in 8.0 mol/L urea extracted from the inclusion bodies was directly injected into the WAX column. The aggregation was prevented and the soluble form of renatured rhRnR in aqueous solution was obtained after desorption from the column. Effects of the extracting solutions, the pH values and urea concentrations in the mobile phase, as well as the sample size on the refolding and purification of rhRnR were investigated, indicating that the above mentioned factors had remarkable influences on the efficiency of refolding, purification and mass recovery of rhRnR. Under the optimal conditions, rhRnR was successfully refolded and purified simultaneously by WAX in one step within only 30 min. The result was satisfactory with mass recovery of 71.8% and purity of 94.8%, which was further tested by western blotting. The specific binding of the purified rhRnR to recombinant human renin was also determined using surface plasmon resonance (SPR). The association constant of rhRnR to recombinant human renin was calculated to be 3.25 × 10⁸ L/mol, which demonstrated that rhRnR was already renatured and simultaneously purified in one step using WAX. All of the above demonstrate that protein folding liquid chromatography (PFLC) should be a powerful tool for the purification and renaturation of rhRnR. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:864–871, 2014     

Immobilized Triton X-100-assisted refolding of Green Fluorescent Protein-Tobacco Etch Virus protease fusion protein using β-cyclodextrin as the eluent

A new protein refolding technique based on the use of the non-charged detergent Triton X-100 immobilized to the cross-linked agarose gel Sepharose High Performance has been developed. The new solid phase was used in combination with soluble β-cyclodextrin (β-CD) to refold recombinant Green Fluorescent Protein fused to Tobacco Etch Virus protease (GFPTEVP) expressed as inclusion bodies in E. coli. Previous attempts to refold recombinant GFPTEVP by dilution had failed. In the new procedure a column packed with Triton X-100-coupled Sepharose High Performance was used to capture unfolded GFPTEVP followed by elution using an increasing β-CD concentration gradient. The yield of properly refolded GFPTEVP was 46% at a protein concentration of 380 μg/ml. In contrast, dilution refolding of GFPTEVP at 200 μg/ml refolding buffer resulted in only 4.7% of native protein.     

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.     

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%.     

PURIFICATION AND BIOLOGICAL CHARACTERIZATION OF BACTERIALLY EXPRESSED RECOMBINANT BUFFALO PROLACTIN

Recombinant prolactin (PRL) from water buffalo (Bubalus bubalis) has been cloned and expressed in a prokaryotic expression system. The hormone was also successfully refolded into a biologically active form. Total RNA was purified from buffalo pituitaries and the buPRL cDNA was synthesized using primers designed on bovine PRL sequence. This prolactin cDNA was cloned in a pET 28a vector and expressed in Escherichia coli strain BL21(DE3)pLysS. Most of the expressed protein was present as insoluble inclusion bodies. The inclusion bodies were solubilized and buPRL was purified by Ni-NTA column. The purified protein was refolded by gradually decreasing the concentration of denaturant during dialysis. Total yield of the refolded and soluble prolactin was 22 mg/L from 100 mL bacterial culture in LB medium. The recombinant prolactin was as active as native prolactin in stimulating growth of Nb2 lymphoma cells.     

Expression and purification of HtpX-like small heat shock integral membrane protease of an unknown organism related to Methylobacillus flagellatus

The M48 conserved family of peptidases contains a single catalytic zinc ion tetrahedrally co-ordinated by two histidines within an HEXXH motif. The proteases of this class are generally toxic to the cell and thus difficult to express and purify. Here, we report the expression and purification of the small HtpX-like heat shock metalloprotease from an unknown organism related to the obligate methylotrophic anaerobic bacterium, Methylobacillus flagellatus. The protease was expressed in the Escherichia coli vector — pT7. Optimization of expression was done to increase the yield and solubility of the expressed protein. Improved refolding procedures from inclusion bodies of pT7 E. coli system were devised to get the protease in an active and stable form. The protease was purified to near homogeneity in its active form from the refolded proteins of the inclusion bodies by a two-step (cation exchange followed by gel filtration) high performance liquid chromatography (HPLC). The purified protease was active on zymography and casein hydrolysis assays. The activity of the protease was found to be optimum at pH 7.4 and at a temperature of 37 °C but significant activity was also retained at higher temperatures of 45–50 °C. Centrifugal fractionation showed that it is a membrane localized endopeptidase. The methods described here can serve as guidelines to express and purify other homologues of M48 family of proteases for functional and structural studies.     

A multipurpose fusion tag derived from an unstructured and hyperacidic region of the amyloid precursor protein

Expression and purification of aggregation‐prone and disulfide‐containing proteins in Escherichia coli remains as a major hurdle for structural and functional analyses of high‐value target proteins. Here, we present a novel gene‐fusion strategy that greatly simplifies purification and refolding procedure at very low cost using a unique hyperacidic module derived from the human amyloid precursor protein. Fusion with this polypeptide (dubbed FATT for Flag‐Acidic‐Target Tag) results in near‐complete soluble expression of variety of extracellular proteins, which can be directly refolded in the crude bacterial lysate and purified in one‐step by anion exchange chromatography. Application of this system enabled preparation of functionally active extracellular enzymes and antibody fragments without the need for condition optimization.     

Purification and characterization of recombinantStreptomyces clavuligerus isopenicillin N synthase produced inEscherichia coli

Recombinant isopenicillin N synthase fromStreptomyces clavuligerus was produced in the form of inactive inclusion bodies inEscherichia coli. These inclusion bodies were solubilized by treatment with 5 M urea under reducing conditions. Optimization of refolding conditions to recover active isopenicillin N synthase indicated that a dialysis procedure carried out at a protein concentration of about 1.0 mg ml^–1 gave maximal recovery of active isopenicillin N synthase. Solubilized isopenicillin N synthase of more than 95% purity was obtained by passing this material through a DEAE-Trisacryl ion exchange column. Expression studies conducted at different temperatures indicated that isopenicillin N synthase was produced predominantly in a soluble, active form when expression was conducted at 20°C, and accounted for about 20% of the total soluble protein. This high-level production facilitated the purification of soluble isopenicillin N synthase to near homogeneity in four steps. Characterization of the purified soluble and solubilized isopenicillin N synthase revealed that they are very similar.     

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.     

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