融合牛肠激酶轻链EKL包涵体蛋白的复性纯化

大肠杆菌高密度发酵表达肠激酶轻链融合蛋白DsbA-rEKL,主要以包涵体形式存在。包涵体经4mol/L尿素和0.5%TritonX-100洗涤,以6mol/L盐酸胍、100mmol/LDTT溶解,在胱氨酸存在下,以脉冲加样方式复性。融合蛋白复性在6mmol/L胱氨酸存在下、脉冲加量0.03mg/mL和复性终蛋白浓度0.3mg/mL为最佳复性方案。复性的融合蛋白加2mmol/LCaCL2后快速自切。经IDA-Sepharose及Q-Sepharose纯化,rEKL纯度可达95%以上,可高效酶切重组瑞特普酶融合蛋白Trx-rPA。实现了大规模生产rEKL,每升发酵液经复性及纯化后,可得rEKL60mg/L以上,使以融合蛋白表达rPA等药用蛋白成为现实。     

Effects of solutes on solubilization and refolding of proteins from inclusion bodies with high hydrostatic pressure

High hydrostatic pressure (HHP)-mediated solubilization and refolding of five inclusion bodies (IBs) produced from bacteria, three gram-negative binding proteins (GNBP1, GNBP2, and GNBP3) from Drosophila, and two phosphatases from human were investigated in combination of a redox-shuffling agent (2 mM DTT and 6 mM GSSG) and various additives. HHP (200 MPa) combined with the redox-shuffling agent resulted in solubilization yields of approximately 42%-58% from 1 mg/mL of IBs. Addition of urea (1 and 2 M), 2.5 M glycerol, L-arginine (0.5 M), Tween 20 (0.1 mM), or Triton X-100 (0.5 mM) significantly enhanced the solubilization yield for all proteins. However, urea, glycerol, and nonionic surfactants populated more soluble oligomeric species than monomeric species, whereas arginine dominantly induced functional monomeric species (approximately 70%-100%) to achieve refolding yields of approximately 55%-78% from IBs (1 mg/mL). Our results suggest that the combination of HHP with arginine is most effective in enhancing the refolding yield by preventing aggregation of partially folded intermediates populated during the refolding. Using the refolded proteins, the binding specificity of GNBP2 and GNBP3 was newly identified the same as with that of GNBP1, and the enzymatic activities of the two phosphatases facilitates their further characterization.     

An efficient refolding method for the preparation of recombinant human prethrombin-2 and characterization of the recombinant-derived alpha-thrombin

Human recombinant prethrombin-2 was produced in Escherichia coli. The expressed prethrombin-2 formed intracellular inclusion bodies from which the protein was refolded by a simple one-step dilution process in buffer consisting of 50 mM Tris-HCl, containing 20 mM CaCl(2), 500 mM NaCl, 1 mM EDTA, 600 mM arginine, 1 mM cysteine, 0.1 mM cystine, 10% (v/v) glycerol, and 0.2% (w/v) Brij-58 at pH 8.5. After refolding, prethrombin-2 was purified by hirudin-based COOH-terminal peptide affinity chromatography, and then activated with Echis carinatus snake venom prothrombin activator (ecarin). The activated protein, alpha-thrombin, was then tested for several activities including activity toward chromogenic substrate, release of fibrinopeptide A from fibrinogen, activation of protein C, and thrombin-activatable fibrinolysis inhibitor, reactivity with antithrombin, clotting activity, and platelet aggregation. The kinetic data showed no differences in activity between our recombinant alpha-thrombin and plasma-derived alpha-thrombin. The yield of refolded recombinant human prethrombin-2 was about 4-7% of the starting amount of solubilized protein. In addition, the final yield of purified refolded protein was 0.5-1%, and about 1 mg of recombinant prethrombin-2 could be isolated from 1 liter of E. coli cell culture.     

The refolding, purification, and activity analysis of a rice Bowman-Birk inhibitor expressed in Escherichia coli

A putative rice trypsin/chymotrypsin inhibitor of the Bowman-Birk family, RBBI-8 of about 20 kDa, was expressed in Escherichia coli as a fusion protein bearing an N-terminal (His)6 purification tag. The expressed recombinant protein, rRBBI-8, is insoluble and accumulates as inclusion bodies. The insoluble protein was solubilized in 8 M urea under reducing environment and then refolded into its active conformation under optimized redox conditions. Strategies used to optimize yield and efficiency include selecting the redox system, increasing protein concentration during refolding by adding the denatured protein in a stepwise way, utilizing additives to prevent aggregation, and selecting buffer-exchanging conditions. A Ni-chelate affinity column was then employed to purify the renatured protein. rRBBI-8 shows strong inhibitory activity against trypsin and it can slightly inhibit chymotrypsin. In this study, a refolding and purification system was set up for this cysteine-rich recombinant protein expressed in a prokaryotic system.     

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.     

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.     

High‐throughput protein refolding screening method using zeolite

We established a 96‐well‐plate‐based refolding screening system using zeolite. In this system, protein denatured and solubilized with 6 M guanidine hydrochloride is adsorbed onto zeolite placed in a 96‐well plate. The refolding conditions can be tested by incubating the samples with refolding buffers under various conditions of pH, salts, and additives. In this study, we chose green fluorescent protein as the model protein. Green fluorescent protein was expressed as inclusion bodies, and we tested the effects of four pH conditions and six additives on its refolding. The results demonstrate that green fluorescent protein was more efficiently refolded with zeolite than with the conventional dilution method. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Refolding of the Fusion Protein of Recombinant Enterokinase Light Chain rEKL

The fusion protein of enterokinase light chain, DsbA-rEK_L, was expressed mainly in the inclusion body in E. coli. The recombinant bacteria were fermented to high density, with high expression of the fusion protein. After being washed with 0.5 % Triton X-100 and 4 mol/L urea, the inclusion body was dissolved in 6 mol/L guanidine and 100 mmol/L DTT, derivatized by cystine and refolded by pulse refolding. The strategy of pulse refolding involved the addition of 0.03 mg/mL of fusion protein until its final concentration reached 0.3 mg/mL. The refolded protein was autocleaved, and the active EK_L molecule was released after the addition of 2 mmol/L of CaCl₂. Using the two-step purification processes of IDA-Sepharose chromatography and Q-Sepharose chromatography, the purity of rEK_L was found to be above 95 %, with a high activity to cleave the recombinant reteplase fusion protein, Trx-rPA. The yield of purified rEK_L was more than 60 mg/L of cultures. As a result, the therapeutic proteins like rPA could be produced on a large scale in a way such as expressed in the form of fusion proteins.     

Substitution of serine for non-disulphide-bond-forming cysteine in grass carp (Ctenopharygodon idellus) growth hormone improves in vitro oxidative renaturation

Native grass carp (Ctenopharygodon idellus) growth hormone, has 5 cysteine amino acid residues, forms two disulphide bridges in its mature form. Recombinant grass carp growth hormone, when over-expressed in E. coli, forms inclusion bodies. In vitro oxidative renaturation of guanidine-hydrochloride dissolved recombinant grass carp growth hormone was achieved by sequential dilution and stepwise dialysis at pH 8.5. The redox potential of the refolding cocktail was maintained by glutathione disulphide/glutathione couple. The oxidative refolded protein is heterogeneous, and contains multimers, oligomers and monomers. The presence of non-disulphide-bond-forming cysteine in recombinant grass carp growth hormone enhances intermolecular disulphide bond formation and also nonnative intramolecular disulphide bond formation during protein folding. The non-disulphide-bond-forming cysteine was converted to serine by PCR-mediated site-directed mutagenesis. The resulting 4-cysteine grass carp growth hormone has improved in vitro oxidative refolding properties when studied by gel filtration and reverse phase chromatography. The refolded 4-cysteine form has less hydrophobic aggregate and has only one monomeric isoform. Both refolded 4-cysteine and 5-cysteine forms are active in radioreceptor binding assay.     

Refolding by High Pressure of a Toxin Containing Seven Disulfide Bonds: Bothropstoxin-1 from <Emphasis Type="Italic">Bothrops jararacussu</Emphasis>

Aggregation is a serious obstacle for recovery of biologically active heterologous proteins from inclusion bodies (IBs) produced by recombinant bacteria. E. coli transformed with a vector containing the cDNA for Bothropstoxin-1 (BthTx-1) expressed the recombinant product as IBs. In order to obtain the native toxin, insoluble and aggregated protein was refolded using high hydrostatic pressure (HHP). IBs were dissolved and refolded (2 kbar, 16 h), and the effects of protein concentration, as well as changes in ratio and concentration of oxido-shuffling reagents, guanidine hydrochloride (GdnHCl), and pH in the refolding buffer, were assayed. A 32% yield (7.6 mg per liter of bacterial culture) in refolding of the native BthTx-1 was obtained using optimal conditions of the refolding buffer (Tris–HCl buffer, pH 7.5, containing 3 mM of a 2:3 ratio of GSH/GSSG, and 1 M GdnHCl). Scanning electron microscopy (SEM) showed that that disaggregation of part of IBs particles occurred upon compression and that the morphology of the remaining IBs, spherical particles, was not substantially altered. Dose-dependent cytotoxic activity of high-pressure refolded BthTx-1 was shown in C2C12 muscle cells.     

Expression, purification, and bioactivity of human tumstatin from Escherichia coli

Tumstatin is a M(r) 28,000 C-terminal NC1 fragment of type alpha3 (IV) collagen that inhibits pathological angiogenesis and suppresses proliferation of endothelial cells and growth of tumors. We report here high cytoplasmic expression of recombinant human tumstatin in Escherichia coli and its purification, in vitro refolding, and inhibitory activity analysis. Human tumstatin was expressed in the bacterial cytoplasm as an insoluble N-terminal polyhistidine tagged protein, which accounted for more than 30% of total bacterial protein in BL21 (DE3) cells. After extraction and solubilization in guanidine-HCl, recombinant protein was purified to homogeneity using a simple one-step Ni(2+)-chelate affinity chromatography and then refolded by dialysis against acidic pH buffers with gradually decreasing concentrations of denaturant. The renatured recombinant tumstatin could specifically inhibit endothelial cell proliferation in a dose-dependent manner, and suppress bFGF-induced angiogenesis in chick embryo chorioallantoic membrane and tumor growth in mouse B16 melanoma xenograft models.     

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.     

Studies on the Refolding Process of Recombinant Horseradish Peroxidase

Horseradish peroxidase (HRP) is an important heme-containing glyco-enzyme that has been used in many biotechnological fields. Valuable proteins like HRP can be obtained in sufficient amounts using Escherichia coli as an expression system. However, frequently, the expression of recombinant enzyme results in inclusion bodies, and the refolding yield is generally low for proteins such as plant peroxidases. In this study, a recombinant HRP was cloned and expressed in the form of inclusion bodies. Initially, the influence of few additives on HRP refolding was assessed by the one factor at a time method. Subsequently, factors with significant effects including glycerol, GSSG/DTT, and the enzyme concentration were selected for further optimization by means of the central composite design of response surface methodology (RSM). Under the obtained optimal condition, refolding increased about twofold. The refolding process was then monitored by the intrinsic fluorescence intensity under optimal conditions (0.35 mM GSSG, 0.044 mM DTT, 7 % glycerol, 1.7 M urea, and 2 mM CaCl₂ in 20 mM Tris, pH 8.5) and the reconstitution of heme to the refolded peroxidase was detected by the Soret absorbance. Additionally, samples under unfolding and refolding conditions were analyzed by Zetasizer to determine size distribution in different media.     

Renaturation of cobra venom phospholipase A2 expressed from a synthetic gene in Escherichia coli.

Cobra venom (Naja naja naja) phospholipase A2 (PLA2) contains 14 cysteines in the form of 7 disulfide bonds amongst its 119 amino acids. A gene encoding the PLA2 was synthesized and inserted into a bacterial expression vector containing the phage lambda pL promoter. In order to obtain protein without the initiating methionine at the N-terminus, a Factor Xa site was engineered upstream from the PLA2 gene. Upon heat-induction of the cells transformed with the expression plasmid, the protein is produced as insoluble inclusion bodies. The enzyme was partially purified by washing the inclusion bodies with Triton X-100 and urea. The expressed protein was first denatured with 8 M guanidine-HCl and 10 mM DTT. After digestion with Factor Xa, formation of disulfide bonds and refolding into the fully active form was carried out in the presence of cysteine and Ca2+. The renatured recombinant protein was purified by Affi-gel blue column chromatography. The purified recombinant enzyme had the same specific activity as the native enzyme when assayed on a variety of substrates and cross-reacted with antisera prepared against the native enzyme. This is the first report of the expression of a recombinant PLA2 from any venom.     

In vitro splicing of erythropoietin by the Mycobacterium tuberculosis RecA intein without substituting amino acids at the splice junctions

Protein splicing is a self-catalyzed process involving the excision of an intervening polypeptide sequence, the intein, and joining of the flanking polypeptide sequences, the extein, by a peptide bond. We have studied the in vitro splicing of erythropoietin (EPO) using a truncated form of the Mycobacterium tuberculosis RecA mini-intein in which the homing endonuclease domain was replaced with a hexahistidine sequence (His-tag). The intein was inserted adjacent to cysteine residues to assure that the spliced product had the natural amino acid sequence. When expressed in Escherichia coli, intein-containing EPO was found entirely as inclusion bodies but could be refolded in soluble form in the presence of 0.5 M arginine. Protein splicing of the refolded protein could be induced with a reducing agent such as DTT or tris(2-carboxyethyl)phosphine and led to the formation of EPO and mini-intein along with some cleavage products. Protein splicing mediated by the RecA intein requires the presence of a cysteine residue adjacent to the intein insertion site. We compared the efficiencies of protein splicing adjacent to three of the four cysteine residues of EPO (Cys29, Cys33 and Cys161) and found that insertion of intein adjacent to Cys29 allowed far more efficient protein splicing than insertion adjacent to Cys33 or Cys161. For ease of purification, our experiments involved a His-tagged EPO fusion protein and a His-tagged intein and the spliced products (25 kDa EPO and 24 kDa mini-intein) were identified by Western blotting using anti-EPO and anti-His-tag antibodies and by mass spectroscopy. The optimal splicing yield at Cys29 (40%) occurred at pH 7.0 after refolding at 4 degrees C and splicing for 18 h at 25 degrees C in the presence of 1 mM DTT.     

Techno-economic evaluation of an inclusion body solubilization and recombinant protein refolding process

Expression of recombinant proteins in Escherichia coli is normally accompanied by the formation of inclusion bodies (IBs). To obtain the protein product in an active (native) soluble form, the IBs must be first solubilized, and thereafter, the soluble, often denatured and reduced protein must be refolded. Several technically feasible alternatives to conduct IBs solubilization and on-column refolding have been proposed in recent years. However, rarely these on-column refolding alternatives have been evaluated from an economical point of view, questioning the feasibility of their implementation at a preparative scale. The presented study assesses the economic performance of four distinct process alternatives that include pH induced IBs solubilization and protein refolding (pH_IndSR); IBs solubilization using urea, dithiothreitol (DTT), and alkaline pH followed by batch size-exclusion protein refolding; inclusion bodies (IBs) solubilization using urea, DTT, and alkaline pH followed by simulated moving bed (SMB) size-exclusion protein refolding, and IBs solubilization using urea, DTT and alkaline pH followed by batch dilution protein refolding. The economic performance was judged on the basis of the direct fixed capital, and the production cost per unit of product (P(C)). This work shows that (1) pH_IndSR system is a relatively economical process, because of the low IBs solubilization cost; (2) substituting β-mercaptoethanol for dithiothreithol is an attractive alternative, as it significantly decreases the product cost contribution from the IBs solubilization; and (3) protein refolding by size-exclusion chromatography becomes economically attractive by changing the mode of operation of the chromatographic reactor from batch to continuous using SMB technology.     

Structural studies on acid unfolding and refolding of recombinant human interferon gamma

Interferon gamma is distinguished from other types of interferons in its instability upon acid treatment, as demonstrated by a loss of antiviral activity. Acid unfolding and refolding experiments were performed with recombinant DNA derived human interferon gamma. When the protein was subjected to unfolding and refolding, the refolded protein showed two peaks (peaks I and II) in gel filtration which have been shown to differ in size, structure, and antiviral activity. When the smaller, peak II, form was unfolded by dialysis against 0.01 M HCl containing 0.1 M NaCl (pH 2) and refolded by dialysis against various solvents at neutral pH, it re-formed as peak II but also generated peak I, and the ratio of the two forms was dependent on protein concentration and solvent conditions. Higher protein concentrations and higher ionic strength led to a greater ratio of peak I to peak II. Phosphate buffers caused precipitation of peak I. Since peak II is 4-8 times more active than peak I in the antiviral bioassay, generation of peak I by acid treatment of peak II should lead to a decrease in antiviral activity.     

Expression, purification, and characterization of the 4 zinc finger region of human tumor suppressor WT1

Wilm's Tumor gene 1 (WT1) encodes a zinc finger protein with four distinct splice isoforms. WT1 has a critical role in genesis of various cancer types both at the DNA/RNA and the protein level. The zinc-finger DNA-binding capacity of the protein is located in the C-terminal domain. Two recombinant proteins, 6HIS-ZN-wt1 and 6HIS-ZN+wt1, corresponding to two alternative splice variants of the C-terminal regions of human WT1 (-KTS) and WT1 (+KTS), respectively, were over-expressed with hexa-histidine fusion tags in inclusion bodies in Escherichia coli for crystallization studies. A combination of Ni2+-NTA affinity and size-exclusion chromatography was applied for purification of the proteins in denaturing conditions. The effects of various buffers, salts and other additives were scrutinized in a systematic screening to establish the optimal conditions for solubility and refolding of the recombinant WT1 proteins. Circular dichroism analysis revealed the expected betabetaalpha content for the refolded proteins, with a notable degradation of the alpha-helical segment in the DNA-free state. Electrophoretic mobility shift assay with double-stranded DNA containing the double Egr1 consensus site 5'-GCG-TGG-GCG-3' confirmed that 6HIS-ZN-wt1 has higher DNA binding affinity than 6HIS-ZN+wt1.     

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%.     

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.