Improving the refolding of NTA protein by urea gradient and arginine gradient size-exclusion chromatography

Inclusion body refolding processes play a major role in the production of recombinant proteins. Improvement of the size-exclusion chromatography refolding process was achieved by combining a decreasing urea gradient with an increasing arginine gradient (two gradients) for the refolding of NTA protein (a new thrombolytic agent) in this paper. Different refolding methods and different operating conditions in two gradients gel filtration process were investigated with regard to increasing the NTA protein activity recovery and inhibition of aggregation. The refolding of denatured NTA protein showed this method could significantly increase the activity recovery of protein at high protein concentration. The activity recovery of 37% was obtained from the initial NTA protein concentration up to 20 mg/ml. The conclusions presented in this study could also be applied to the refolding of lysozyme.     

Mechanism of pH‐sensitive polymer‐assisted protein refolding and its application in TGF‐β1 and KGF‐2

Refolding of proteins at high concentrations often results in non‐productive aggregation. This study, through a unique combination of spectroscopic and chromatographic analyzes, provides biomolecular evidence to demonstrate the ability of Eudragit S‐100, a pH‐responsive polymer, to enhance refolding of denatured‐reduced lysozyme at high concentrations. The addition of Eudragit in the refolding buffer significantly increases lysozyme refolding yield to 75%, when dilution refolding was conducted at 1 mg/mL lysozyme. This study shows evidence of an electrostatic interaction between oppositely charged lysozyme and the Eudragit polymer during refolding. This ionic complexing of Eudragit and lysozyme appears to shield exposed hydrophobic residues of the lysozyme refolding intermediates, thus minimizing hydrophobic‐driven aggregation of the molecules. Importantly, results from this study show that the Eudragit‐lysozyme bioconjugation does not compromise refolded protein structure, and that the polymer can be readily dissociated from the protein by ion exchange chromatography. The strategy was also applied to refolding of TGF‐β1 and KGF‐2. © 2009 American Institute of Chemical Engineers Biotechnol. Prog. 2009     

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

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

Refolding 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     

Chaperone and antichaperone activities of trigger factor.

Reduced denatured lysozyme tends to aggregate at neutral pH and competition between productive folding and aggregation substantially reduces the efficiency of refolding. Trigger factor, a folding catalyst and chaperone can, depending on the concentration of trigger factor and the solution conditions, cause either a substantial increase (chaperone activity) or a substantial decrease (antichaperone activity) in the recovery of native lysozyme as compared with spontaneous refolding. When trigger factor is working as a chaperone, the reactivation rates of lysozyme are decelerated and aggregation decreases with increasing trigger factor concentrations. Under conditions where antichaperone activity of trigger factor dominates, the reactivation rates of lysozyme are accelerated and aggregation is increased. Trigger factor and lysozyme were both released from the aggregates on re-solubilization with urea indicating that trigger factor participates directly in aggregate formation and is incorporated into the aggregates. The apparently dual effect of trigger factor toward refolding of lysozyme is a consequence of the peptide binding ability and may be important in regulation of protein biosynthesis.     

蛋白质二硫键异构酶相关蛋白A的表达及性质的研究

克隆了Aspergillus niger T21中的蛋白质二硫键异构酶相关蛋白A（PRPA）基因,并将它插入pET23b表达载体。在E. coli中表达时,PRPA占菌体总蛋白的34%。经过超声破细胞、硫酸铵分级沉淀和离子交换层析获得了纯度大于90%的重组蛋白。PRPA有二硫键异构酶活性。在PRPA存在下,变性和还原的溶菌酶复性率和复性速度降低,电泳结果表明溶菌酶聚集增多。荧光结果表明PRPA表面有较多的疏水基团。     

Refolding of superoxide dismutase by ion-exchange chromatography

A new ion-exchange chromatography process was developed for refolding of iron superoxide dismutase (Fe-SOD) produced in Escherichia coli as an inclusion body. After adsorption on an ion-exchange matrix, the denatured protein was eluted by gradient decrease of urea concentration and pH of the elution buffer. The dual gradient allowed the denatured protein to refold to its correct native conformation with return of biological activity. Compared with the traditional dilution, refolding process, the new process increased the refolding yield five-fold. The process could also be carried out at high protein concentration to decrease the solution volume after refolding.     

On-column refolding of recombinant human interferon-gamma inclusion bodies by expanded bed adsorption chromatography

A refolding strategy was described for on-column refolding of recombinant human interferon-gamma (rhIFN-gamma) inclusion bodies by expanded bed adsorption (EBA) chromatography. After the denatured rhIFN-gamma protein bound onto the cation exchanger of STREAMLINE SP, the refolding process was performed in expanded bed by gradually decreasing the concentration of urea in the buffer and the refolded rhIFN-gamma protein was recovered by the elution in packed bed mode. It was demonstrated that the denatured rhIFN-gamma protein could be efficiently refolded by this method with high yield. Under appropriate experimental conditions, the protein yield and specific activity of rhIFN-gamma was up to 52.7% and 8.18 x 10(6) IU/mg, respectively.     

Statistical optimization and multiple objective programming of lysozyme refolding catalyzed by recombinant DsbA in vitro

DsbA (disulfide bond formation protein A) is essential for disulfide bond formation directly affecting the nascent peptides folding to the correct conformation in vivo. In this paper, recombinant DsbA protein was employed to catalyze denatured lysozyme refolding and inhibit the aggregation of folding intermediates in vitro. Statistical methods, i.e., Plackett–Burman design and small central composite design, were adopted to screen out important factors affecting the refolding process and correlating these parameters with the refolding efficiency including both protein recovery and specific activity of refolded lysozyme. Four important parameters: initial lysozyme concentration, urea concentration, KCl concentration and GSSG (glutathione disulfide) concentration were picked out and operating conditions were optimized by introducing the effectiveness coefficient method and transforming the multiple objective programming into an ordinary constrained optimization issue. Finally, 99.7% protein recovery and 25,600 U/mg specific activity of lysozyme were achieved when 281.35 μg/mL denatured lysozyme refolding was catalyzed by an equivalent molar of DsbA at the optimal settings. The results indicated that recombinant DsbA protein could effectively catalyze the oxidized formation and reduced isomerization of intramolecular disulfide bonds in the refolding of lysozyme in vitro.     

Separation and identification of different refolding components

A dual-gradient ion-exchange chromatography (IEC) refolding process has been successfully applied to renature lysozyme at high concentration. The different refolding components were separated by size-exclusion chromatography with low concentrations of urea and NaCl added into elution buffer. The hydrodynamic characteristics during separation and the hydrophobic properties of these components were also tested.     

Refolding of denatured/reduced lysozyme at high concentration with diafiltration

Refolding of reduced and denatured protein in vitro has been an important issue for both basic research and applied biotechnology. Refolding at low protein concentration requires large volumes of refolding buffer. Among various refolding methods, diafiltration is very useful to control the denaturant and red/ox reagents in a refolding solution. We constructed a refolding procedure of high lysozyme concentration (0.5-10 mg/ml) based on the linear reduction of the urea concentration during diafiltration under oxygen pressure. When the urea concentration in the refolding vessel was decreased from 4 M with a rate of 0.167 M/h, the refolding yields were 85% and 63% at protein concentrations, 5 mg/ml and 10 mg/ml, respectively, after 11 h. This method gave a high productivity of 40.1,microM/h of the refolding lysozyme. The change in refolding yields during the diafiltration could be simulated using the model of Hevehan and Clark.     

Ion-exchange resins greatly facilitate refolding of like-charged proteins at high concentrations

Protein refolding is a crucial step for the production of therapeutic proteins expressed in bacteria as inclusion bodies. In vitro protein refolding is severely impeded by the aggregation of folding intermediates during the folding process, so inhibition of the aggregation is the most effective approach to high‐efficiency protein refolding. We have herein found that electrostatic repulsion between like‐charged protein and ion exchange gel beads can greatly suppress the aggregation of folding intermediates, leading to the significant increase of native protein recovery. This finding is extensively demonstrated with three different proteins and four kinds of ion‐exchange resins when the protein and ion‐exchange gel are either positively or negatively charged at the refolding conditions. It is remarkable that the enhancing effect is significant at very high protein concentrations, such as 4 mg/mL lysozyme (positively charged) and 2 mg/mL bovine serum albumin (negatively charged). Moreover, the folding kinetics is not compromised by the presence of the resins, so fast protein refolding is realized at high protein concentrations. It was not realistic by any other approaches. The working mechanism of the like‐charged resin is considered due to the charge repulsion that could induce oriented alignment of protein molecules near the charged surface, leading to the inhibition of protein aggregation. The molecular crowding effect induced by the charge repulsion may also contribute to accelerating protein folding. The refolding method with like‐charged ion exchangers is simple to perform, and the key material is easy to separate for recycling. Moreover, because ion exchangers can work as adsorbents of oppositely charged impurities, an operation of simultaneous protein refolding and purification is possible. All the characters are desirable for preparative refolding of therapeutic proteins expressed in bacteria as inclusion bodies. Bioeng. 2011; 108:1068–1077. © 2010 Wiley Periodicals, Inc.     

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%.     

层析辅助体外复性含有多对二硫键的融合蛋白质

为建立一种基于阴离子交换介质辅助的含多对二硫键的抗凝溶栓双功能水蛭素12肽-瑞替普酶融合蛋白质 (HV12p-rPA) 的复性方法,采用Q Sepharose XL作为层析复性介质,通过正交实验考察蛋白质上样量、流速、脲梯度、洗脱液中精氨酸浓度、脲浓度、pH、还原型及氧化型谷胱甘肽等因素对复性过程的影响,探索最佳层析复性条件。结果表明：脲梯度、上样量及精氨酸浓度是影响复性的3个主要因素。脲梯度是复性成功的关键,上样量增大时复性蛋白质比活降低,精氨酸辅助HV12p-rPA复性的最佳浓度为1 mol/L。创建了脲、pH双梯度下的阴离子交换层析辅助HV12p-rPA的复性方法,复性后蛋白质的溶栓比活达到46 520 IU/mg,抗凝比活达到9 980 ATU/mg,与稀释复性方法相比,该方法能使复性蛋白质的溶栓比活提高14~15倍,抗凝比活提高7~8倍。     

Initial protein concentration and residual denaturant concentration strongly affect the batch refolding of hen egg white lysozyme

The effects of several variables on the refolding of hen egg white lysozyme have been studied. Lysozyme was denatured in both urea, and guanidine hydrochloride (GuHCl), and batch refolded by dilution (100 to 1000 fold) into 0.1M Tris-HCl, pH 8.2, 1 mM EDTA, 3 mM reduced glutathione and 0.3 mM oxidised glutathione. Refolding was found to be sensitive to temperature, with the highest refolding yield obtained at 50°C. The apparent activation energy for lysozyme refolding was found to be 56 kJ/mol. Refolding by dilution results in low concentrations of both denaturant and reducing agent species. It was found that the residual concentrations obtained during dilution (100-fold dilution: [GuHCl]=0.06 mM, [DTT]=0.15 mM) were significant and could inhibit lysozyme refolding. This study has also shown that the initial protein concentration (1–10 mg/mL) that is refolded is an important parameter. In the presence of residual GuHCl and DTT, higher refolding yields were obtained when starting from higher initial lysozyme concentrations. This trend was reversed when residual denaturant components were removed from the refolding buffer.     

Continuous refolding of lysozyme with fed-batch addition of denatured protein solution

A continuous refolding method with addition of denatured protein solution in a fed-batch manner through a ceramic membrane tube was developed. Denatured and fully reduced lysozyme was continuously refolded with high refolding efficiencies. In this method, a denatured lysozyme solution was gradually added from the outer surface of the membrane tube into a refolding buffer flowing continuously inside the tube under controlled mixing conditions. The refolding efficiencies of lysozyme in this continuous refolding were higher than those in a batch dilution method. This method has applicability to large-scale downstream processes and can attain a high efficiency and protein concentration in refolding. Refolded proteins can be supplied continuously following purification steps.     

Operational regimes for a simplified one-step artificial chaperone refolding method

The "artificial chaperone method" for protein refolding developed by Rozema et al. (Rozema, D.; Gellman, S. H. J. Am. Chem. Soc. 1995, 117 (8), 2373-2374) involves the sequential dilution of denatured protein into a buffer containing detergent (cetyltrimethylammonium bromide, CTAB) and then into a refolding buffer containing cyclodextrin (CD). In this paper a simplified one-step artificial chaperone method is reported, whereby CTAB is added directly to the denatured solution, which is then diluted directly into a refolding buffer containing beta-cyclodextrin (beta-CD). This new method can be applied at high protein concentrations, resulting in smaller processing volumes and a more concentrated protein solution following refolding. The increase in achievable protein concentration results from the enhanced solubility of CTAB at elevated temperatures in concentrated denaturant. The refolding yields obtained for the new method were significantly higher than for control experiments lacking additives and were comparable to the yields obtained with the classical two-step approach. A study of the effect of beta-CD and CTAB concentrations on refolding yield suggested two operational regimes: slow stripping (beta-CD/CTAB approximately 1), most suited for higher protein concentrations, and fast stripping (beta-CD/CTAB approximately 2.7), best suited for lower protein concentrations. An increased chaotrope concentration resulted in higher refolding yields and an enlarged operational regime.     

Effects of protein conformational changes on separation performance in electrostatic interaction chromatography: unfolded proteins and PEGylated proteins

As it is important to understand how protein conformational changes affect the separation performance in ion exchange chromatography (IEC), we investigated two model systems, unfolded proteins (lysozyme and bovine serum albumin) with urea and dithiothreitol, and PEGylated proteins (lysozyme attached with polyethyleneglycol molecular weight 5000). Linear gradient elution IEC experiments were carried out and the data were analysed by our model previously presented in order to obtain the binding site value B and the peak salt concentration I(R). Unfolded proteins (bovine serum albumin and lysozyme) with urea and dithiothreitol showed weaker retention and larger binding site values compared with the values for native proteins. Multiple PEGylated lysozyme peaks were separated, and eluted earlier than the native peak appeared. There is a good correlation between B and I(R) for PEGylated lysozymes.     

Cycloamylose as an efficient artificial chaperone for protein refolding

High molecular weight cyclic alpha-1,4-glucan (referred to as cycloamylose) exhibited an artificial chaperone property toward three enzymes in different categories. The inclusion properties of cycloamylose effectively accommodated detergents, which keep the chemically denatured enzymes from aggregation, and promoted proper protein folding. Chemically denatured citrate synthase was refolded and completely recovered it's enzymatic activity after dilution with polyoxyethylenesorbitan buffer followed by cycloamylose treatment. The refolding was completed within 2 h, and the activity of the refolded citrate synthase was quite stable. Cycloamylose also promoted the refolding of denatured carbonic anhydrase B and denatured lysozyme of a reduced form.     

Predictions of matrix‐assisted refolding of α‐lactalbumin: Process efficiency versus batch dilution method

Protein refolding is an important technique to produce active recombinant proteins from inclusion bodies. Because of the complexity of the refolding process, a trial‐and‐error method is usually used for its design, which is ineffective and time consuming. Therefore, an efficient method for the process prediction is indispensable to optimize the operating conditions. In this article, we suggest a design procedure for matrix‐assisted protein refolding. Three different chromatographic techniques were considered exploiting hydrophobic interaction chromatography, ion‐exchange chromatography, and SEC media. The procedure consisted of quantification of refolding kinetics, analysis of the retention behavior of all protein forms involved in refolding, construction of a dynamic model, and the process simulation. Denatured bovine α‐lactalbumin was used as model protein. The refolding rate was measured for different protein concentration using the batch dilution method. A kinetic scheme for the protein refolding was suggested and incorporated into a dynamic model of chromatographic column and used for predicting the refolding performance. The productivity, yield, and buffer consumption were used as performance indicators for the refolding techniques considered. The matrix‐assisted protein refolding process outperformed batch dilution method with respect to all indicators provided that efficient method for the process design was used.