Improved solubilization of recombinant human growth hormone inclusion body produced in Escherichia coli

Recombinant human growth hormone (r-hGH) overexpressed in Escherichia coli forms inactive and insoluble aggregates as inclusion bodies in the cytoplasm. The efficient solubilization of inclusion bodies is critical for cost-effective production. Contrary to a previous report, in our production system, the solubilization method by alkaline treatment including 2 M urea was ineffective. Hence various buffers containing different concentrations of urea or guanidine hydrochloride (GnHCl) at neutral and alkaline pH were attempted. Efficient solubilization (about 90%) was observed in 100 mM Tris buffer, pH 8.0, with more than 4 M GnHCl, and at pH 12.5 with more than 2 M GnHCl, but not with about 8 M of urea. The r-hGH solubilized at pH 12.5 containing 2 M GnHCl was refolded by simple dilution and purified by DEAE Sepharose anion-exchange chromatography. The biological activity of the resulting r-hGH was comparable with commercially available r-hGH in in vitro cell proliferation assay using the hGH-dependent cell line.     

Optimization of inclusion body solubilization and renaturation of recombinant human growth hormone from Escherichia coli

Recombinant human growth hormone (r-hGH) was expressed in Escherichia coli as inclusion bodies. In 10 h of fed-batch fermentation, 1.6 g/L of r-hGH was produced at a cell concentration of 25 g dry cell weight/L. Inclusion bodies from the cells were isolated and purified to homogeneity. Various buffers with and without reducing agents were used to solubilize r-hGH from the inclusion bodies and the extent of solubility was compared with that of 8 M urea as well as 6 M Gdn-HCl. Hydrophobic interactions as well as ionic interactions were found to be the dominant forces responsible for the formation of r-hGH inclusion bodies during its high-level expression in E. coli. Complete solubilization of r-hGH inclusion bodies was observed in 100 mM Tris buffer at pH 12.5 containing 2 M urea. Solubilization of r-hGH inclusion bodies in the presence of low concentrations of urea helped in retaining the existing native-like secondary structures of r-hGH, thus improving the yield of bioactive protein during refolding. Solubilized r-hGH in Tris buffer containing 2 M urea was found to be less susceptible to aggregation during buffer exchange and thus was refolded by simple dilution. The r-hGH was purified by use of DEAE-Sepharose ion-exchange chromatography and the pure monomeric r-hGH was finally obtained by using size-exclusion chromatography. The overall yield of the purified monomeric r-hGH was approximately 50% of the initial inclusion body proteins and was found to be biologically active in promoting growth of rat Nb2 lymphoma cell lines.     

Expression,refolding and purification of a human interleukin-17A variant

A human interleukin-17A (IL-17A) variant was overexpressed in Escherichia coli BL21 (DE3) under the control of a T₇ promoter. The resulting insoluble inclusion bodies were isolated and solubilized by homogenization with 6 M guanidine HCl. The denatured recombinant human IL-17A variant was refolded in 20 mM Tris–HCl, pH 9.0, 500 mM arginine, 500 mM guanidine HCl, 15% glycerol, 1 mM cystamine, and 5 mM cysteine at 2–8 °C for 40 h. The refolded IL-17A variant was subsequently purified using a combination of cation-exchange, reversed-phase and fluoroapatite chromatography. The final purified product was a monodisperse and crystallizable homodimer with a molecular weight of 30,348.3 Da. The protein was active in both receptor binding competition assay and IL-17A-dependent biological activity assay using human dermal fibroblasts.     

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.     

An efficient in vitro refolding of recombinant bacterial laccase in Escherichia coli

Laccases (benzenediol oxygen oxidoreductases, EC 1.10.3.2) are important multicopper enzymes that are used in many biotechnological processes. A recombinant form of laccase from Bacillus sp. HR03 was overexpressed in Escherichia coli BL-21(DE3). Inclusion body (IB) formation happens quite often during recombinant protein production. Hence, developing a protocol for efficient refolding of proteins from inclusion bodies to provide large amounts of active protein could be advantageous for structural and functional studies. Here, we have tried to find an efficient method of refolding for this bacterial enzyme. Solubilization of inclusion bodies was carried out in phosphate buffer pH 7, containing 8 M urea and 4 mM β-mercaptoethanol and refolding was performed using the dilution method. The effect of different additives was investigated on the refolding procedure of denaturated laccase. Mix buffer (phosphate buffer and citrate buffer, 100 mM) containing 4 mM ZnSO₄ and 100 mM sorbitol was selected as an optimized refolding buffer. Also Kinetic parameters of soluble and refolded laccase were analyzed.     

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.     

Expression of recombinant human cathepsin K is enhanced by codon optimization

A synthetic codon-optimized gene encoding human procathepsin K has been cloned in Escherichia coli using pET28a+ vector. The recombinant His-tagged fusion protein was expressed as inclusion body, solubilized in urea and purified by metal affinity chromatography. The purified protein was refolded by dilution technique, concentrated and finally purified by gel-filtration chromatography. The expressed protein was confirmed by Western blot analysis with human cathepsin K specific antibody. We have obtained 140 mg purified and refolded protein from 1 L bacterial culture which is the highest (nearly three times higher) yield reported so far for a recombinant human procathepsin K. The protease could be autocatalytically activated to mature protease at lower pH in presence of cysteine protease specific activators. The recombinant protease showed gelatinolytic and collagenolytic activities as well as activity against synthetic substrate Z-FR-AMC with a K_m value of 5 ± 2.7 μM and the proteolytic activity of the enzyme could be blocked by cysteine protease inhibitors E-64, leupeptin and MMTS.     

Recovery of active N-acetyl-D-glucosamine 2-epimerase from inclusion bodies by solubilization with non-denaturing buffers

Overexpression of recombinant N-acetyl-d-glucosamine 2-epimerase, one of the key enzymes for the synthesis of N-acetylneuraminic acid, in E. coli led to the formation of protein inclusion bodies. In this study we report the recovery of active epimerase from inclusion bodies by direct solubilization with Tris buffer. At pH 7.0, 25% of the inclusion bodies were solubilized with Tris buffer. The specific activity of the solubilized proteins, 2.08 ± 0.02 U/mg, was similar to that of the native protein, 2.13 ± 0.01 U/mg. The result of circular dichroism spectroscopy analysis indicated that the structure of the solubilized epimerase obtained with pH 7.0 Tris buffer was similar to that of the native epimerase purified from the clarified cell lysate. As expected, the extent of deviation in CD spectra increased with buffer pH. The total enzyme activity recovered by solubilization from inclusion bodies, 170.41 ± 10.06 U/l, was more than 2.5 times higher than that from the clarified cell lysate, 67.32 ± 5.53 U/l. The results reported in this study confirm the hypothesis that the aggregation of proteins into inclusion bodies is reversible and suggest that direct solubilization with non-denaturing buffers is a promising approach for the recovery of active proteins from inclusion bodies, especially for aggregation-prone multisubunit proteins.     

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.     

Purification and efficient refolding process for recombinant tissue-type plasminogen activator derivative (reteplase) using glycerol and Tranexamic acid

In this study, a novel and economic method for refolding and purifying recombinant tissue plasminogen activator derivative (r-PA; reteplase) was developed. Reteplase with nine disulfide bonds in its complex structure is expressed in the form of inclusion bodies in Escherichia coli and requires tedious dissolving and refolding processes to achieve its biological activity. Among the different refolding additives that were evaluated, glycerol and tranexamic acid (Txa) were found to be more effective in increasing the refolding yield of reteplase. Using response surface methodology, a solution containing 3.5 M urea, 33% (v/v) glycerol, and 400 mM Txa was found to give the highest refolding yield. The synergic effect of urea, glycerol, and Txa under optimum conditions for a reteplase concentration of 25 μg ml⁻¹ resulted in a high refolding yield of 76.41%. Increased reteplase concentration in the refolding buffer was achieved using the pulse-fed method. In the pulse-fed method, a refolding yield of 49.53% was achieved for a final reteplase concentration of 300 μg ml⁻¹. Using Txa as a novel refolding aid for reteplase instead of ionic amino acids like l-Arginine allowed to purify the refolded reteplase directly by cation-exchange chromatography with high purity.     

Expression and biochemical analysis of codon-optimized polyphenol oxidase from Camellia sinensis (L.) O. Kuntze in E. coli

Polyphenol oxidases (PPOs) are copper-containing industrially important enzymes that catalyze the synthesis of many commercially important products by using polyphenols as substrate. Camellia sinensis polyphenol oxidase (CsPPO) is interesting because it oxidizes epicatechins to yield theaflavins and thearubigins. The present study aimed to optimize the expression of CsPPO in Escherichia coli. Because CsPPO had a large number of E. coli rare codons, it yielded a poor quantity of protein in E. coli Rosetta™ 2 cells, which have additional tRNAs for E. coli rare codons. Thus, synthetically constructed codon-optimized CsPPO was cloned into pET-47b(+) vector and expressed in a bacterial host. Ectopic expression led to the formation of inclusion bodies. However, extensive standardization of buffers and methods of refolding such as dialysis, on-column refolding, and rapid dilution yielded active PPO from solubilized inclusion bodies with copper content of 0.880 ± 0.095 atom/molecule of protein.Experimental data produced maximum PPO activity in a rapid dilution buffer containing 0.5 M L-arginine. Refolded CsPPO had an optimum pH of 5.0 and K_m values of 3.10, 0.479, and 0.314 mM, and a V_max of 163.9, 82.64, and 142.8 U/mg of protein for catechol, catechin, and epicatechin, respectively.     

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.     

Purification effect of artificial chaperone in the refolding of recombinant ribonuclease A from inclusion bodies

Artificial chaperone (AC) containing cetyltrimethylammonium bromide (CTAB) and β-cyclodextrin (β-CD) has been used to refold recombinant ribonuclease A (RNase A) from inclusion bodies (IBs). At low urea concentration (0.8 M), the AC could enhance the refolding yield of RNase A by effectively suppressing its intermolecular interaction-induced aggregation. As a result, 0.9 mg/mL RNase A could be 77% refolded, which was a 57% increase as compared to that without the AC. At high protein concentration range (0.9–2.3 mg/mL in total protein concentrations) and 1.6 M urea, CTAB selectively precipitated contaminant proteins distinctly, so a purification effect was achieved. For example, 1.5 mg/mL RNase A could be 62% refolded and recovered at a purity of 87%, which was a 34% increase in purity as compared to that in IBs (65%). The precipitation selectivity was considered due to the differences in the hydrophobicity of the proteins. The work indicates that by using the AC, RNase A could be efficiently refolded at low urea concentration and purified at high urea concentration from IBs at high protein concentrations.     

Employment of colorimetric enzyme assay for monitoring expression and solubility of GST fusion proteins targeted to inclusion bodies

High levels of recombinant protein expression can lead to the formation of insoluble inclusion bodies. These complex aggregates are commonly solubilized in strong denaturants, such as 6–8 M urea, although, if possible, solubilization under milder conditions could facilitate subsequent refolding and purification of bioactive proteins. Commercially available GST-tag assays are designed for quantitative measurement of GST activity under native conditions. GST fusion proteins accumulated in inclusion bodies are considered to be undetectable by such assays. In this work, solubilization of recombinantly produced proteins was performed in 4 M urea. The activity of rGST was assayed in 2 M urea and it was shown that rGST preserves 85% of its activity under such denaturing conditions. A colorimetric GST activity assay with 1-chloro-2, 4-dinitrobenzene (CDNB) was examined for use in rapid detection of expression targeted to inclusion bodies and for the identification of inclusion body proteins which can be solubilized in low concentrations of chaotropic agents. Applicability of the assay was evaluated by tracking protein expression of two GST-fused allergens of biopharmaceutical value in E. coli, GST-Der p 2 and GST-Mus a 5, both targeted to inclusion bodies.     

Interferon-α 2b quantification in inclusion bodies using Reversed Phase-Ultra Performance Liquid Chromatography (RP-UPLC)

Interferon-α 2b (IFN-α 2b) is a recombinant therapeutic cytokine produced as inclusion bodies using a strain of Escherichia coli as expression system. After fermentation and recovery, it is necessary to know the amount of recombinant IFN-α 2b, in order to determine the yield and the load for solubilization, and chromatographic protein purification steps. The present work details the validation of a new short run-time and fast sample-preparation method to quantify IFN-α 2b in inclusion bodies using Reversed Phase-Ultra Performance Liquid Chromatography (RP-UPLC). The developed method demonstrated an accuracy of 100.28%; the relative standard deviations for method precision, repeatability and inter-day precision tests were found to be 0.57%, 1.54% and 1.83%, respectively. Linearity of the method was assessed in the range of concentrations from 0.05 mg/mL to 0.5 mg/mL, the curve obtained had a determination coefficient (r²) of 0.9989. Detection and quantification limits were found to be 0.008 mg/mL and 0.025 mg/mL, respectively. The method also demonstrated robustness for changes in column temperature, and specificity against host proteins and other recombinant protein expressed in the same E. coli strain.     

Expression,purification, phosphorylation and characterization of recombinant human statherin

This work reports the successful recombinant expression of human statherin in Escherichia coli, its purification and in vitro phosphorylation. Human statherin is a 43-residue peptide, secreted by parotid and submandibular glands and phosphorylated on serine 2 and 3. The codon-optimized statherin gene was synthesized and cloned into commercial pTYB11 plasmid to allow expression of statherin as a fusion protein with intein containing a chitin-binding domain. The plasmid was transformed into E. coli strains and cultured in Luria–Bertani medium, which gave productivity of soluble statherin fusion protein of up to 47 mg per liter of cell culture, while 112 mg of fusion protein were in the form of inclusion bodies. No significant refolded target protein was obtained from inclusion bodies. The amount of r-h-statherin purified by RP–HPLC corresponded to 0.6 mg per liter of cell culture. Attenuated total reflection-Fourier transform infrared spectroscopy experiments performed on human statherin isolated from saliva and r-h-statherin assessed the correct folding of the recombinant peptide. Recombinant statherin was transformed into the diphosphorylated biologically active form by in vitro phosphorylation using the Golgi-enriched fraction of pig parotid gland containing the Golgi-casein kinase.     

Expression, Purification, and Refolding of Active Recombinant Human E-selectin Lectin and EGF Domains in Escherichia coli

Attempts to obtain active E-selectin from Escherichia coli (E. coli) have not yet been successful. In this study, we succeeded in expressing the recombinant lectin and epidermal growth factor domain fragments of human E-selectin (rh-ESLE) in E. coli on a large-scale. The rh-ESLE protein was expressed as an inactive form in the inclusion bodies. The inactive form of rh-ESLE was denatured and solubilized by 6 M guanidine hydrochloride and then purified by Ni²⁺ affinity chromatography under denaturing conditions. Denatured rh-ESLE was then refolded by a rapid-dilution method using a large amount of refolding buffer, which contained arginine and cysteine/cystine. The refolded rh-ESLE showed binding affinity for sLe^X (K _d = 321 nM, B_max = 1.9 pmol/μg protein). This result suggests that the refolded rh-ESLE recovered its native and functional structure.     

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     

Refolding and two-step purification by hydrophobic interaction chromatography of recombinant human bone morphogenetic protein-2 from Escherichia coli

To renature the inactive rhBMP-2 which overexpressed in Escherichia coli, post-expression treatments including inclusion bodies solubilization and in vitro refolding were systematically investigated. An optimized refolding process was established from screening and successfully scaled up with yield greater than 70%. Then, hydrophobic interaction chromatography (HIC) was adopted as two consecutive stages to separate the active rhBMP-2 homodimer from refolding mixture. Aiding additive N,N-dimethylformamide (DMF) was found to enhance the resolution of rhBMP-2 homodimer most effectively. The rhBMP-2 homodimer was purified to homogeneity through two HIC separations at different salt contents, the purified rhBMP-2 homodimer was fully bioactive and had equivalent biological activity to rhBMP-2 produced from Chinese hamster ovary cell (CHO). Under the optimal refolding and purification conditions, 80 mg rhBMP-2 homodimer with high purity could be obtained from 1 g wet weight of inclusion bodies. Finally, this efficient refolding and purification procedure was successfully scaled up in the pilot pharmaceutical plant.     

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.