Increased yield of high purity recombinant human interferon-gamma utilizing reversed phase column chromatography

Increasing therapeutic applications for recombinant human interferon-gamma (rhIFN-gamma), an antiviral proinflammatory cytokine, has broadened interest in optimizing methods for its production and purification. We describe a reversed phase chromatography (RPC) procedure using Source-30 matrix in the purification of rhIFN-gamma from Escherichia coli that results in a higher yield than previously reported. The purified rhIFN-gamma monomer from the RPC column is refolded in Tris buffer. Optimal refolding occurs at protein concentrations between 50 and 100 microg/ml. This method yields greater than 90% of the dimer form with a yield of 40 mg/g cell mass. Greater than 99% purity is achieved with further purification over a Superdex G-75 column to obtain specific activities of from 2 x 10(7) to 4 x 10(7)IU/mg protein as determined via cytopathic antiviral assay. The improved yield of rhIFN-gamma in a simple chromatographic purification procedure promises to enhance the development and therapeutic application of this biologically potent molecule.     

On-column refolding of recombinant human interferon-gamma with an immobilized chaperone fragment

The chaperone mini-GroEL is a soluble recombinant fragment containing the 191-345 amino acid sequence of GroEL with a 6xHis tag. The refolding protocol assisted with mini-GroEL was studied for the activity recovery of rhIFN-gamma inclusion bodies. In a suspended system, mini-GroEL showed significant enhancement of the activity recovery of rhIFN-gamma, applyed with a 1-5:1 stoichiometry of mini-GroEL to rhIFN-gamma at 25 degrees C. Moreover, 1 M urea in the renaturation buffer had a synergistic effect on suppressing the aggregation and improving the activity recovery. Finally, a novel chromatographic column, containing 1 cm height of Sephadex G 200 at the top of column and packed with immobilized mini-GroEL to promote refolding, was devised. The total activity recovered per milligram of denatured rhIFN-gamma was up to 3.93 x 10(6) IU with the immobilized mini-GroEL column, which was reused four times without evident loss of renaturation ability. A convenient technique with the integrated process of chaperon preparation and rhIFN-gamma folding in vitro was developed.     

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.     

重组人粒细胞-巨噬细胞集落刺激因子复性和纯化方法的比较

比较重组人粒细胞-巨噬细胞集落刺激因子(rhGM-CSF)在用疏水色谱(HIC)、离子交换色谱(IEC)和体积排阻色谱(SEC)3种液相色谱进行复性和纯化,选择较好的复性和纯化方法.通过对比rhGM-CSF在液相色谱上复性和纯化的主要指标,包括比活、纯度和质量回收率,结果发现采用HIC和IEC对rhGM-CSF进行复性和纯化时,其比活可以达到国家标准,纯度和质量回收率也比较高,而采用SEC,其比活、纯度和质量回收率远低于HIC和IEC.     

Renaturation and purification of rhGM-CSF with ion-exchange chromatography

The renaturation and purification of recombinant human granulocyte macrophage colony stimulation factor (rhGM-CSF) expressed in Escherichia coli with strong anion-exchange chromatography (SAX) were studied. The effects of pH values, ratios of concentrations of GSH/GSSG, and urea concentrations in the mobile phase on the renaturation and purification of rhGM-CSF with SAX were investigated, respectively. The results show that the above three factors have remarkable influences on the efficiency of renaturation and mass recovery of rhGM-CSF. The addition of GSH/GSSG in the mobile phase can improve the formation of correct disulfide bonds in rhGM-CSF so that its renaturation yield increases. In addition, to enhance the mass recovery of rhGM-CSF with SAX, the low concentration of urea was added in the mobile phase to prevent denatured protein aggregation. Under the optimal conditions, rhGM-CSF was renatured with simultaneous purification on SAX column within 30 min only by one step. After that its specific bioactivity, mass recovery, and purity reached 1.66 x 10(7) IU x mg, 58.8%, and 96.2%, respectively.     

huGM-CSF(9-127)-IL-6(29-184)融合蛋白的复性及纯化研究

利用Q Sepharose H.P.离子交换柱层析在8mol/L尿素变性条件下对huGM-CSF(9-127)-IL-6(29-184）融合蛋白进行初步纯化,然后再利用Sephacryl S-200分子筛柱层析复性及纯化后获得目的蛋白,其纯度达到95％以上。该纯化方案成功地解决了稀释复性或透析复性产物在进行Q Sepharose H.P.离子交换柱层析时目的蛋白不稳定而沉积于柱上的问题,获得了较好的复性效果,复性率达到80％以上。使用该纯化方案,1天内便可基本完成重组蛋白的复性及纯化过程,而且也便于扩大。     

Optimized procedure for renaturation of recombinant human bone morphogenetic protein-2 at high protein concentration

The human gene encoding the mature form of bone morphogenetic protein-2 (hBMP-2), a dimeric disulfide-bonded protein of the cystine knot growth factor family, was expressed in recombinant Escherichia coli using a temperature-inducible expression system. The recombinant protein was produced in the form of cytoplasmic inclusion bodies and the effect of different variables on the renaturation of rhBMP-2 was investigated. In particular, variables such as pH, redox conditions, protein concentration, temperature, the presence of different types of aggregation suppressors, and host cell contaminants were studied with respect to their effect on aggregation during refolding and on the final renaturation yield of rhBMP-2. It is shown that the renaturation yield is particularly sensitive to pH, temperature, protein concentration, and the presence of aggregation suppressors. In contrast, little effect of the redox conditions and the ionic strength on the renaturation yield was observed, as equal yields were obtained in a broad range of reduced to oxidized glutathione ratios and concentrations of NaCl, respectively. The aggregation suppressor 2-(cyclohexylamino)ethanesulfonic acid (CHES) proved to be superior with respect to the final renaturation yield, although, in comparison to the more common arginine, it was less efficient in preventing aggregation of rhBMP-2 during refolding. Detergent washing of inclusion bodies was sufficient, as further purification of rhBMP-2 prior to refolding was without effect on the final renaturation yield. An increase in the concentration of renatured rhBMP-2 was achieved by a pulsed refolding procedure by which up to a total amount of 2.1 mg mL(-1) rhBMP-2 could be transferred in seven pulses into the renaturation buffer with an overall refolding yield of 38%, corresponding to 0.8 mg mL(-1) renatured dimeric rhBMP-2. Furthermore, a simplified purification procedure is presented that also includes freeze-drying for long-term storage of biologically active rhBMP-2. Finally, it is shown that the appearance of rhBMP-2 variants could be avoided by using a host strain overexpressing rare codon tRNAs.     

Improving purification of recombinant human interferon gamma expressed in Escherichia coli; effect of removal of impurity on the process yield

Process development and optimization studies were performed in order to improve the purification process of (rhIFN-gamma). The objective was to generate material with higher purity and quantity. An in-process control screening was developed to obtain the optimal condition for column chromatographic purification by measuring LPS, nucleic acids, rhIFN- gamma, monomer and its covalent dimers. A new resin screening method was applied to select optimal resin for each of the chromatographic columns. The resulting process used Butyl and Q-Sepharose, refolding and SP-Sepharose for purification of IFN-gamma. Effects of different process conditions such as cell lysis, removal of impurity and oxygen concentration were evaluated. Removal of impurities was evaluated by washing of inclusion bodies with 1% Triton X-100 and 3M urea and different chromatography steps. The results reveal that Triton removed about 43% of the LPS but urea had no effect on removal of nucleic acids and LPS. Further analysis show that removal of impurities by column chromatography decreases aggregation and increases the process yield. Oxygen concentration was identified as parameter that could have a significant impact on covalent dimers formation, as an unacceptable pharmaceutical form of rhIFN-gamma. On the basis of small-scale studies, optimum operating conditions were chosen and the purification process was successfully scaled-up to a pilot scale process with step yield and product quality that were better than previous reports.     

蛋白的色谱复性及同时纯化

对近年来新发展的用液相色谱(LC)进行蛋白质复性及同时纯化的方法做了评述,详细介绍了蛋白质在4种液相色谱上的复性及同时纯化的方法、设备和影响因素,并对各自的优缺点进行了比较,为色谱法作为研究蛋白质折叠及用于基因工程生产治疗蛋白质的复性及同时纯化技术的进一步应用提供依据。     

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%.     

An approach for increasing the mass recovery of proteins derived from inclusion bodies in biotechnology

A method for increasing the mass recovery of therapeutic proteins produced by E. coli using liquid chromatography was investigated. Recombinant human interferon-gamma (rhIFN-gamma) produced by E. coli was selected as a model therapeutic protein, and hydrophobic interaction chromatography (HIC) was performed as a model for liquid chromatography. Using seven types of stationary phase hydrophobic interaction chromatography (STHIC) with different end groups, the effect of the stationary phase on the mass recovery during protein folding by liquid chromatography (LC) and the causes of mass loss of rhIFN-gamma during its folding with simultaneous purification were investigated. Also strategies for increasing mass recovery are proposed. The results demonstrate that the mass recovery of rhIFN-gamma increases with the decreasing hydrophobicity for six STHIC with end groups of PEG-200, PEG-400, PEG-600, PEG-1000, furfural, and phenyl, except for PEG-1000. However, for oxethyl and PEG-600, even though the same diol end group is bonded to PEG-600, so long as the PEG-600 is modified by acetyl chloride, it can effectively enhance the mass and bioactivity recovery of rhIFN-gamma compared to the PEG-600 column. The effect of sample size including both mass and volume on the mass recovery of the rhIFN-gamma was also investigated. Last, redissolving the target protein that has irreversibly adsorbed to the stationary phase and re-injecting it onto the column is an approach for increasing mass recovery.     

Renaturation of Escherichia coli-derived recombinant human macrophage colony-stimulating factor.

Recombinant human macrophage colony-stimulating factor (rhM-CSF), a homodimeric, disulfide bonded protein, was expressed in Escherichia coli in the form of inclusion bodies. Reduced and denatured rhM-CSF monomers were refolded in the presence of a thiol mixture (reduced and oxidized glutathione) and a low concentration of denaturing agent (urea or guanidinium chloride). Refolding was monitored by nonreducing gel electrophoresis and recovery of bioactivity. The effects of denaturant type and concentration, protein concentration, concentration of thiol/disulfide reagents, temperature, and presence of impurities on the kinetics of rhM-CSF renaturation were investigated. Low denaturant concentrations (<0.5 M urea) and high protein concentrations (>0.4 mg/ml) in the refolding mixture resulted in increased formation of aggregates, although aggregation was never significant even when refolding was carried out at room temperature. Higher protein concentration resulted in higher rates but did not lead to increased yields, due to the formation of unwanted aggregates. Experiments conducted at room temperature resulted in slightly higher rates than those conducted at 4 degrees C. Although the initial renaturation rate for solubilized inclusion body protein without purification was higher than that of the reversed-phase purified reduced denatured rhM-CSF, the final renaturation yield was much higher for the purified material. A maximum refolding yield of 95% was obtained for the purified material at the following refolding conditions: 0.5 M urea, 50 mM Tris, 1.25 mM DTT, 2 mM GSH, 2 mM GSSG, 22 degrees C, pH 8, [protein] = 0.13 mg/ml.     

Efficient and easily scalable protein folding strong anion exchange chromatography for renaturation and simultaneous purification of recombinant human asparaginase from E. coli

Recombinant proteins are revolutionizing present day therapeutics. They are generally expressed as insoluble inclusion bodies in the E. coli and mis‐folding, loss of protein, and high cost of down streaming are the hurdles in their recovery. For the first time, we are reporting the refolding with simultaneous purification of rhASP in E. coli using a single step utilizing protein folding‐strong anion exchange chromatography (PF‐SAX). The purification method is also standardized for optimal concentration of solution additives, pH, and mobile phase composition. The results showed purification of rhASP with anion exchange chromatography was effective. Phosphate buffer and slightly alkaline pH produced significant recovery yields and purity profiles. The effect of solution additives such as arginine, glycerol, TMAO, sorbitol, dextran, glutamate, and fructose on rhASP renaturation is also investigated. Significant results were achieved using arginine‐TMAO combination in terms of purity, recovery yield and specific activity of 99%, 78%, and 210 IU/mg, respectively. The work concludes that PF‐SAX refolding method is superior to other conventional methods and it can be applied to large scale purification of rhASP produced in E. coli. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:1036–1044, 2018     

Oxidative renaturation of lysozyme at high concentrations

Newly synthesized cloned gene proteins expressed in bacteria frequently accumulate in insoluble aggregates or inclusion bodies. Active protein can be recovered by solubilization of inclusion bodies followed by renaturation of the solubilized (unfolded) protein. The recovery of active protein is highly dependent on the renaturation conditions chosen. The renaturation process is generally conducted at low protein concentrations (0.01-0.2 mg/mL) to avoid aggregation. We have investigated the potential of successfully refolding reduced and denatured hen egg white lysozyme at high concentrations (1 and 5 mg/mL). By varying the composition of the renaturation media, optimum conditions which kinetically favor proper folding over inactivation were found. Solubilizing agents such as guanidinium chloride (GdmCl) and folding aids such as L-arginine present in low concentrations during refolding effectively enhanced renaturation yields by suppressing aggregation resulting in reactivation yields as high as 95%. Quantitatively the kinetic competition between lysozyme folding and aggregation can be described using first-order kinetics for the renaturation reaction and third-order kinetics for the overall aggregation pathway. The rate constants for both reactions have been found to be strongly dependent on denaturant and thiol concentration. This strategy supercedes the necessity to reactivate proteins at low concentrations using large renaturation volumes. The marked increase in volumetric productivity makes this a viable option for recovering biologically active protein efficiently and in high yield in vitro from proteins produced as inclusion bodies within microbial cells. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 221-230, 1997.     

RGD-葡激酶的凝胶过滤层析法复性及其纯化

构建的溶栓和抗栓双重功能的RGD-葡激酶突变体(RGD-Sak)在大肠杆菌中高表达,目的蛋白质以包涵体形式存在。为获得有活性的蛋白质,需要对包涵体进行变复性。利用凝胶层析方法对包涵体中RGD-Sak进行复性,并与稀释复性法进行比较,发现凝胶柱复性方法具有操作周期短、简便、成本低而高效等优点。复性后蛋白质用Q-Sepharose FF离子交换进一步纯化,纯度达95%,酪蛋白凝胶板活性测定表明两种复性法得到的蛋白质比活性相当。圆二色谱测定显示两种复性法得到的蛋白质的二级结构成份和谱形一致,说明在两种复性过程中完成了RGD-Sak分子的正确折叠。     

Refolding and purification of yeast carboxypeptidase Y expressed as inclusion bodies in Escherichia coli

The genes encoding carboxypeptidase Y (CPY) and CPY propeptide (CPYPR) from Saccharomyces cerevisiae were cloned and expressed in Escherichia coli. Six consecutive histidine residues were fused to the C-terminus of the CPYPR for facilitated purification. High-level expression of CPY and CPYPR-His(6) was achieved but most of the expressed proteins were present in the form of inclusion bodies in the bacterial cytoplasm. The CPY and CPYPR-His(6) produced as inclusion bodies were separated from the cells and solubilized in 6 and 3 M guanidinium chloride, respectively. The denatured CPYPR-His(6) was refolded by dilution 1:30 into the renaturation buffer (50 mM Tris-HCl containing 0.5 M NaCl and 3 mM EDTA, pH 8.0), and the refolded CPYPR-His(6) was further purified to 90% purity by single-step immobilized metal ion affinity chromatography. The denatured CPY was refolded by dilution 1:60 into the renaturation buffer containing CPYPR-His(6) at various concentrations. Increasing the molar ratio of CPYPR-His(6) to CPY resulted in an increase in the CPY refolding yield, indicating that the CPYPR-His(6) plays a chaperone-like role in in vitro folding of CPY. The refolded CPY was purified to 92% purity by single-step p-aminobenzylsuccinic acid affinity chromatography. When refolding was carried out in the presence of 10 molar eq CPYPR-His(6), the specific activity, N-(2-furanacryloyl)-l-phenylalanyl-l-phenylalanine hydrolysis activity per milligram of protein, of purified recombinant CPY was found to be about 63% of that of native S. cerevisiae CPY.     

A comparative analysis of rapid methods for purification and refolding of recombinant bovine prion protein

Bacterially-produced recombinant prion protein (rPrP) is a frequently used model system for the study of the properties of wild-type and mutant prion proteins by biochemical and biophysical approaches. A range of approaches have been developed for the purification and refolding of untagged rPrP expressed as inclusion bodies in Escherichia coli, including refolding by dialysis and simultaneous on-column purification and refolding. In order to perform a higher-throughput analysis of different rPrP proteins, an approach that produces highly pure rPrP with a minimum of purification steps and a high yield per liter of induced bacterial culture is desired. Here, we directly compare purification approaches for untagged bovine rPrP as adapted to rapid, small-scale formats useful for higher-throughput studies. An analysis of protein yield, purity, oxidation, and refolding revealed significant differences between preparative methods as adapted to the small-scale format, and based on these findings we provide recommendations for future purifications. We also describe the utility of a sensitive commercial kit for thiol analysis of these preparations, the pH dependence of dimer formation during refolding of bovine rPrP, and bovine rPrP binding to cobalt affinity resin.     

蛋白质复性技术研究进展

评述了蛋白质复性研究的科学背景及蛋白质折叠机制的研究现状 ,详细介绍近年来蛋白质复性技术的研究进展 ,包括稀释添加技术和各种辅助因子的作用、固定化辅助因子应用、尺寸排阻色谱和固定化辅助因子色谱等。     

A simplified bioprocess for human alpha-fetoprotein production from inclusion bodies

A simple and effective Escherichia coli (E. coli) bioprocess is demonstrated for the preparation of recombinant human alpha-fetoprotein (rhAFP), a pharmaceutically promising protein that has important immunomodulatory functions. The new rhAFP process employs only unit operations that are easy to scale and validate, and reduces the complexity embedded in existing inclusion body processing methods. A key requirement in the establishment of this process was the attainment of high purity rhAFP prior to protein refolding because (i) rhAFP binds easily to hydrophobic contaminants once refolded, and (ii) rhAFP aggregates during renaturation, in a contaminant- dependent way. In this work, direct protein extraction from cell suspension was coupled with a DNA precipitation-centrifugation step prior to purification using two simple chromatographic steps. Refolding was conducted using a single-step, redox-optimized dilution refolding protocol, with refolding success determined by reversed phase HPLC analysis, ELISA, and circular dichroism spectroscopy. Quantitation of DNA and protein contaminant loads after each unit operation showed that contaminant levels were reduced to levels comparable to traditional flowsheets. Protein microchemical modification due to carbamylation in this urea-based process was identified and minimized, yielding a final refolded and purified product that was significantly purified from carbamylated variants. Importantly, this work conclusively demonstrates, for the first time, that a chemical extraction process can substitute the more complex traditional inclusion body processing flowsheet, without compromising product purity and yield. This highly intensified and simplified process is expected to be of general utility for the preparation of other therapeutic candidates expressed as inclusion bodies.     

重组抗血红素ScFv包涵体蛋白的复性及纯化研究

抗血红素多二硫键ScFv在大肠杆菌中绝大多数表达产物为包涵体,为了获得可溶性的具有生物活性的ScFv,摸索了不同的复性条件,包括透析法、稀释和层析相结合的方法。研究发现,先对溶解的变性ScFv溶液稀释,进行初步的蛋白质复性,再利用Sephadex G-25凝胶层析进一步复性、降低变性剂浓度和纯化,至少可以得到95％纯度,产率为150mg／L的目标蛋白,通过一次凝胶过滤层析,达到了去除变性剂、复性及纯化ScFv蛋白三种目的,为多二硫键ScFv在大肠杆菌中的表达和纯化提供了一种经济可行的方法。