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.     

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 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.     

Thermolabile antifreeze protein produced in Escherichia coli for structural analysis

Inclusion bodies of recombinant human growth hormone (r-hGH) were isolated from Escherichia coli, enriched and solubilized in 100 mM Tris buffer containing 6 M n-propanol and 2 M urea. Around 4 mg/ml of r-hGH from inclusion bodies were solubilized in 6 M n-propanol-based buffer containing 2 M urea. Existence of native-like secondary structure of r-hGH in 6 M n-propanol solution was confirmed by CD and fluorescence spectra. Solubilized r-hGH was subsequently refolded by pulsatile dilution, purified to homogeneity and found to be functionally active. Tris buffer containing 6 M n-propanol and 2 M urea also effectively solubilized a number of proteins expressed as inclusion bodies in E. coli. Mild solubilization of inclusion body proteins, chaotropic effect of n-propanol at high concentration and kosmotropic effect at lower concentration helped in improved refolding of the solubilized protein. Around 40% of the r-hGH in the form of inclusion body aggregates was refolded into bioactive form while using n-propanol as solubilization agent. Solubilization with 6 M n-propanol solution thus can be a viable alternative for achieving high throughput recovery of bioactive protein from inclusion bodies of E. coli.     

Refolding of recombinant human interferon gamma inclusion bodies in vitro assisted by colloidal thermo-sensitive poly(N-isopropylacrylamide) brushes grafted onto the surface of uniform polystyrene cores

Recombinant human interferon gamma (rhIFN-γ) is a protein with great potential for clinical therapy, but rhIFN-γ expressed in Escherichia coli is usually in the form of insoluble inclusion bodies which should be refolded in vitro. A novel type of hairy particles (PNIPAM-grafted-PS) consisted of submicron polystyrene cores and brushes of thermo-sensitive poly(N-isopropylacrylamide) grafted onto the cores was prepared and then applied to assist the refolding of rhIFN-γ in vitro. Two kinds of PNIPAM-grafted-PS particles with different thickness of brush layer (55 nm and 110 nm) were synthesized, which were spherical shape with good dispersion properties and the LCST was about 33 °C. The effect of thickness of brush layer, particle concentration and temperature on the refolding process was investigated, it was shown that particles with larger thickness of brush layer were more effective and the final rhIFN-γ activity could be up to more than 21 times of that in dilution refolding when initial rhIFN-γ concentration was 50 μg/mL. The optimal refolding condition was the concentration ratio of particle to rhIFN-γ 1:1 and refolding temperature of 15 °C. All results above demonstrated that PNIPAM-grafted-PS particles could assist rhIFN-γ refolding which presented an alternative way to facilitate recombinant protein refolding in vitro.     

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.     

Prevention of aggregate formation through mechanism analysis in refolding of recombinant pertactin from Escherichia coli

Production of natural pertactin for pharmaceutical use is limited by its low abundance. In this study, recombinant pertactin was highly expressed in the form of inclusion bodies in E. coli. However, up to 75% of the soluble turned out as aggregates when refolding by pulse-fed batch dilution. The conceivable route for aggregate formation was proposed as that the C-terminus of partially folded intermediate with a strong hydrophobic core would intertwine with that region of newly added denatured protein, resulting in aggregation between proteins with different folding states. The key factor for prevention of aggregate formation was to improve the synchronization of refolding. For this purpose, flash-batch dilution was conducted at a scale of 5 L and achieved a monomeric refolding yield of above 70%. Aggregates formed were efficiently removed along with impurities by one-step chromatography of Ni-resin. The purity of monomeric pertactin was >98%. An overall yield was 320 mg per liter fermentation liquor with a total recovery of about 59%. The purified protein was characterized by MALDI-TOF, circular dichroism, fluorescence, HPLC and DSC, and showed similar physiochemical properties compared to its natural counterpart. Animal study showed similar immunological responses and antibodies elicited demonstrated a comparable reactivity.     

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.     

Membrane combined with hydrophilic macromolecules enhances protein refolding at high concentration

Membrane technology is important to the development of modern biotechnology. It has the potential to efficiently refold protein at high concentration that is still a challenge for pharmaceutical protein produced from inclusion bodies. This paper dealt with the application of a polysulfone hollow fiber membrane to protein refolding using recombinant human granulocyte colony-stimulating factor (rhG-CSF) as a model protein. Compared with dilution refolding at protein concentration of 1.0 mg/mL, the crossflow membrane system led to a 16% increase in soluble protein recovery, and a 3.3-fold increase in specific bioactivity. Addition of PEG 6 K at 2 g/L could further improve the soluble protein recovery up to 57%, the specific bioactivity up to 2.2 × 10⁸ IU/mL. Addition of dextran at 5 g/L could increase the soluble protein recovery up to 63.6%, the specific bioactivity up to 2.30 × 10⁸ IU/mL. By gently and gradually removing denaturant, ultrafiltration membrane system was demonstrated to be very helpful for protein refolding at high concentration. Combining with hydrophilic macromolecular of PEG or dextran could further increase its efficiency. PEG was able to promote the refolding intermediate of rhG-CSF to transfer into the native structure; whereas dextran could enhance protein refolding mainly by weakening shear stress-induced protein aggregation.     

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.     

High-level production of biologically active chemokines in Escherichia coli

The chemokines eotaxin-1 (CCL11) and eotaxin-2 (CCL24), belonging to the CC chemokines family, play key roles in the inflammatory response, allergic asthma and other diseases. When expressed in Escherichia coli, chemokines are prone to form inclusion bodies devoid of biological activity, and it is hard to refold them properly. Here an expression and purification protocol for high-level production of soluble and biologically active CCL11 and CCL24 in E. coli has been established. A final yield of 8.7 mg/l for CCL11 and 3.9 mg/l for CCL24 has been obtained and the purified proteins were characterized with SDS-PAGE, mass spectrometry and circular dichroism. High binding affinity of purified chemokines with CC chemokine receptor type 3 (CCR3) has been confirmed with surface plasmon resonance (SPR) and the K_D values are 3.7 × 10⁻⁷ M and 3.0 × 10⁻⁷ M, respectively, for CCL11 and CCL24. This report provides a straightforward strategy for the efficient production of soluble and biologically active chemokines in E. coli.     

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 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.     

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.     

Cell-free production and characterisation of human uncoupling protein 1–3

The uncoupling proteins (UCPs) leak protons across the inner mitochondrial membrane, thus uncoupling the proton gradient from ATP synthesis. The main known physiological role for this is heat generation by UCP1 in brown adipose tissue. However, UCPs are also believed to be important for protection against reactive oxygen species, fine-tuning of metabolism and have been suggested to be involved in disease states such as obesity, diabetes and cancer.Structural studies of UCPs have long been hampered by difficulties in sample preparation with neither expression in yeast nor refolding from inclusion bodies in E. coli yielding sufficient amounts of pure and stable protein. In this study, we have developed a protocol for cell-free expression of human UCP1, 2 and 3, resulting in 1 mg pure protein per 20 mL of expression media. Lauric acid, a natural UCP ligand, significantly improved protein thermal stability and was therefore added during purification. Secondary structure characterisation using circular dichroism spectroscopy revealed the proteins to consist of mostly α-helices, as expected. All three UCPs were able to bind GDP, a well-known physiological inhibitor, as shown by the Fluorescence Resonance Energy Transfer (FRET) technique, suggesting that the proteins are in a natively folded state.     

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.     

Modulating the development of E. coli biofilms with 2-aminoimidazoles

The synthesis of a 20 member 2-aminoimidazole/triazole pilot library is reported. Each member of the library was screened for its ability to inhibit or promote biofilm development of either Escherichia coli and Acinetobacter baumannii. From this screen, E. coli-selective 2-aminoimidazoles were discovered, with the best inhibitor inhibiting biofilm development with an IC₅₀ of 13 μM. The most potent promoter of E. coli biofilm formation promoted biofilm development by 321% at 400 μM.     

Improvement of succinate production by overexpression of a cyanobacterial carbonic anhydrase in Escherichia coli

Succinate fermentation was investigated in Escherichia coli strains overexpressing cyanobacterium Anabaena sp. 7120 ecaA gene encoding carbonic anhydrase (CA). In strain BL21 (DE3) bearing ecaA, the activity of CA was 21.8 U mg⁻¹ protein, whereas non-detectable CA activity was observed in the control strain. Meanwhile, the activity of phosphoenolpyruvate carboxylase (PEPC) increased from 0.2 U mg⁻¹ protein to 1.13 U mg⁻¹ protein. The recombinant bearing ecaA reached a succinate yield of 0.39 mol mol⁻¹ glucose at the end of the fermentation. It was 2.1-fold higher than that of control strain which was just 0.19 mol mol⁻¹ glucose. EcaA gene was also introduced into E. coli DC1515, which was deficient in glucose phosphotransferase, lactate dehydrogenase and pyruvate:formate lyase. Succinate yield can be further increased to 1.26 mol mol⁻¹ glucose. It could be concluded that the enhancement of the supply of HCO₃⁻ in vivo by ecaA overexpression is an effective strategy for the improvement of succinate production in E. coli.     

Microbial surface displaying formate dehydrogenase and its application in optical detection of formate

In the present work, NAD⁺-dependent formate dehydrogenase (FDH), encoded by fdh gene from Candida boidinii was successfully displayed on Escherichia coli cell surface using ice nucleation protein (INP) from Pseudomonas borealis DL7 as an anchoring protein. Localization of matlose binding protein (MBP)-INP-FDH fusion protein on the E. coli cell surface was characterized by SDS-PAGE and enzymatic activity assay. FDH activity was monitored through the oxidation of formate catalyzed by cell-surface-displayed FDH with its cofactor NAD⁺, and the production of NADH can be detected spectrometrically at 340 nm. After induction for 24 h in Luria-Bertani medium containing isopropyl-β-d-thiogalactopyranoside, over 80% of MBP-INP-FDH fusion protein present on the surface of E. coli cells. The cell-surface-displayed FDH showed optimal temperature of 50 °C and optimal pH of 9.0. Additionally, the cell-surface-displayed FDH retained its original enzymatic activity after incubation at 4 °C for one month with the half-life of 17 days at 40 °C and 38 h at 50 °C. The FDH activity could be inhibited to different extents by some transition metal ions and anions. Moreover, the E. coli cells expressing FDH showed different tolerance to solvents. The recombinant whole cell exhibited high formate specificity. Finally, the E. coli cell expressing FDH was used to assay formate with a wide linear range of 5–700 μM and a low limit of detection of 2 μM. It is anticipated that the genetically engineered cells may have a broad application in biosensors, biofuels and cofactor regeneration system.     

Improvement of protein stability and enzyme recovery under stress conditions by using a small HSP (tpv-HSP 14.3) from Thermoplasma volcanium

In this study we cloned and expressed a small heat shock protein, tpv-HSP 14.3, from thermoacidophilic archaeon Thermoplasma volcanium. This novel recombinant small heat shock protein was purified to homogeneity and produced a protein band of 14.3 kDa on SDS-polyacrylamide gel. Transmission electron microscopy images of the negatively stained tpv-HSP 14.3 samples showed spherical particles of 13 nm diameter. E. coli cells over expressing tpv-HSP 14.3 endowed the cells with some degree of thermotolerance. After exposure to 52 °C for 120 min, survivability of the E. coli cells expressing tpv-HSP 14.3 was approximately 2.5-fold higher than the control cells. As a molecular chaperone tpv-HSP 14.3 enhanced the thermal stabilization of substrate proteins, pig heart citrate synthase and bovine l-glutamic dehdyrogenase, considerably. The highest protection effect of tpv-HSP 14.3 was observed at 47 °C for pig heart citrate synthase; the remaining activity was 5-fold higher than that of the sample without tpv-HSP 14.3. The tpv-sHSP 14.3 prevented inactivation of bovine l-glutamic dehdyrogenase the most effectively at 53 °C; the residual activity was approximately 2-fold higher than that of the sample heated without tpv-HSP 14.3. However, refolding activity of the tpv-HSP 14.3 was relatively weak for the chemically denatured substrate proteins.