大肠杆菌表达的单链抗体柱复性的研究

对包含体表达的抗乙肝病毒表面抗原（HBsAg）的单链抗体（ScFv）纯化复性进行了探索.尝试了利用金属螯合亲和层析和凝胶层析柱进行柱上在位复性的可行性. 对包含体表达的ScFv进行透析复性与柱复性,比较其相对复性率及蛋白质回收率,发现柱上复性效果优于传统的透析复性.抗HBsAg ScFv经凝胶色谱Sephacyl S-200柱复性的相对复性率为98%, 蛋白质回收率为81%.由于将纯化复性同步进行,简化了操作程序,提高了产品的回收率.     

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。     

包涵体蛋白的分离和色谱法体外复性纯化研究进展

重组蛋白在大肠杆菌中表达多为无活性的包涵体形式,须经洗涤、溶解、复性后才能得到生物活性蛋白。综述了近年来包涵体蛋白分离纯化和复性技术研究进展,重点讨论了色谱法复性技术的应用,包括尺寸排阻色谱、亲和色谱、离子交换色谱、疏水相互作用色谱、固定化脂质体色谱、扩张床吸附色谱的进展情况。     

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.     

Inhibition of aggregation by media selection,sample loading and elution in size exclusion chromatographic refolding of denatured bovine carbonic anhydrase B

The effects of gel media, sample application and elution flowrate on the activity recovery and aggregation in refolding of bovine carbonic anhydrase B (CAB) by size exclusion chromatography (SEC) were investigated. Variation in aggregation was demonstrated visibly by the comparison of refolding profiles under different operating conditions. Some principles with regard to practical application were proposed. Meanwhile, the analysis of relationship between peak resolution and activity recovery provided evidences for the mechanism of size exclusion chromatography protein refolding.     

蛋白质的排阻色谱复性的新进展

外源蛋白在大肠杆菌中高效表达时 ,常常形成不溶的、无活性的包涵体 ,包涵体蛋白的复性是重组蛋白生产过程中的一个技术难题。排阻色谱 (sizeexclusionchromatography ,SEC)用于蛋白复性是一种较新的、适用于任何一种蛋白的方法 ,与常用的稀释复性法相比 ,它能在高的起始蛋白浓度下对蛋白进行复性 ,活性回收率较高 ,同时又能使目标蛋白得到一定程度的纯化。对使用SEC复性的进展进行了评述 ,其内容包括SEC复性的原理及其复性过程中的影响因素 ,并对其未来发展进行了展望。     

Refolding of denatured/reduced lysozyme at high concentrations by artificial molecular chaperone‐ion exchange chromatography

Development of high efficiency and low cost protein refolding methods is a highlighted research focus in biotechnology. Artificial molecular chaperone (AMC) and protein folding liquid chromatography (PFLC) are two attractive refolding methods developed in recent years. In the present work, AMC and one branch of PFLC, ion exchange chromatography (IEC), are integrated to form a new refolding method, artificial molecular chaperone‐ion exchange chromatography (AMC‐IEC). This new method is applied to the refolding of a widely used model protein, urea‐denatured/dithiothreitol‐reduced lysozyme. Many factors influencing the refolding of lysozyme, such as urea concentration, β‐cyclodextrin concentration, molar ratio of detergent to protein, mobile phase flow rate, and type of detergent, were investigated, respectively, to optimize the conditions for lysozyme refolding by AMC‐IEC. Compared with normal IEC refolding method, the activity recoveries of lysozyme obtained by AMC‐IEC were much higher in the investigated range of initial protein concentrations. Moreover, the activity recoveries obtained by using this newly developed refolding method were still quite high for denatured/reduced lysozyme at high initial concentrations. When the initial protein concentration was 200 mg mL^?1, the activity recovery was over 60%. In addition, the lifetime of the chromatographic column during AMC‐IEC was much longer than that during protein refolding by normal IEC. Therefore, AMC‐IEC is a high efficient and low cost protein refolding method. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

High productivity refolding of an inclusion body protein using pulsed-fed size exclusion chromatography

Protein refolding using size exclusion chromatography (SEC) is advantageous over conventional refolding methods in terms of ease of automation, simultaneous purification capabilities, and the non-adsorptive protein–matrix interaction which eliminates steric constraints. Despite these advantages, the widespread use of SEC refolding remains restricted by low process productivity and product concentration bottlenecks. This study aims to address those limitations and exploit SEC advantages for large-scale refolding applications. Specifically, this study reports the development of a pulsed-fed size exclusion chromatography (PF-SEC) refolding platform, which successfully refolded E. coli-derived α-fetoprotein (AFP) to achieve 53% refolding yield at 0.9 mg/ml AFP refolding concentration. AFP was introduced into the column by pulsed injection to increase feed load, while suppressing concentration-induced aggregation. Refolding was initiated by a urea gradient in the column, where the gradient length could be readily adjusted to complement pulsed feeding patterns. AFP refolding productivity with PF-SEC improved by 8- and 64-fold compared to ion-exchange chromatography refolding and pulsed dilution refolding, respectively, at a fixed refolding concentration. Through a unique integration of pulsed feeding and urea gradient development, this new PF-SEC refolding methodology overcomes ‘productivity and concentration’-related disadvantages inherent in SEC, and will be scalable for large-scale protein refolding applications.     

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.     

Protein renaturation with simultaneous purification by protein folding liquid chromatography: recent developments

Protein folding liquid chromatography (PFLC) is a powerful tool for protein refolding with simultaneous purification. We review its recent progress in liquid chromatography and molecular biology, primarily involving the validation of PFLC refolding of proteins containing multiple disulphide bonds, the application of mixed-mode chromatography, PFLC in molecular biology. Representative examples are described.     

Refolding of lysozyme in hydrophobic interaction chromatography: Effects of hydrophobicity of adsorbent and salt concentration in mobile phase

The effects of salt concentration in mobile phase, elution strategy, and hydrophobicity of stationary phase on lysozyme refolding in hydrophobic interaction chromatography (HIC) were investigated. Butyl Sepharose 4 Fast Flow, the least hydrophobic HIC resin among the tested adsorbent, showed the best refolding yield. The binding efficiency of unfolded lysozyme on the adsorbent was maximized when 1 and 0.4 M of initial and final concentration of ammonium sulfate was used in mobile phase, respectively. The optimum gradient strategy for refolding and elution of lysozyme was determined as linear increase of urea concentration to 4M. The optimized condition suggests the less hydrophobic environment than conventionally used salt solutions and HIC resins. Consequently, total refolding yield was improved 1.6 times comparing with optimized dilution-based batch refolding method.     

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。     

Overproduction of single-chain antibodies against human IFN-alpha2B in Escherichia coli and their isolation in biologically active form

The gene encoding mouse single chain antibody (ScFv) against human interferon alpha2b (IFN-alpha2b) was cloned into the plasmid vector under the control of promoter from phage T7 and the recombinant protein was expressed in Escherichia coli as inclusion bodies. After the isolation of inclusion bodies the desired protein containing affinity tail "6His tag" was solubilized and purified under denaturing conditions by immobilized-metal affinity chromatography. The soluble and purified ScFv was obtained by "on column" refolding and the recovery of biological activity were demonstrated. The higher levels of ScFv production for intracellular expression system in comparison with ScFv obtained by secretion were shown. The advantages of described refolding method are simplicity and high efficacy, moreover, refolding using a chromatographic process represents the manufacturable approach because it is easily automated using commercially available materials and preparative chromatography systems and also can be combined with simultaneous purification.     

Systematic optimization of expression and refolding of the Plasmodium falciparum cysteine protease falcipain-2

The Plasmodium falciparum cysteine protease falcipain-2 is a potential new target for antimalarial chemotherapy. In order to obtain large quantities of active falcipain-2 for biochemical and structural analysis, a systematic assessment of optimal parameters for the expression and refolding of the protease was carried out. High-yield expression was achieved using M15(pREP4) Escherichia coli transformed with the pQE-30 plasmid containing a truncated profalcipain-2 construct. Recombinant falcipain-2 was expressed as inclusion bodies, solubilized, and purified by nickel affinity chromatography. A systematic approach was then used to optimize refolding parameters. This approach utilized 100-fold dilutions of reduced and denatured falcipain-2 into 203 different buffers in a microtiter plate format. Refolding efficiency varied markedly. Optimal refolding was obtained in an alkaline buffer containing glycerol or sucrose and equal concentrations of reduced and oxidized glutathione. After optimization of the expression and refolding protocols and additional purification with anion-exchange chromatography, 12 mg of falcipain-2 was obtained from 5 liters of E. coli, and crystals of the protease were grown. The systematic approach described here allowed the rapid evaluation of a large number of expression and refolding conditions and provided milligram quantities of recombinant falcipain-2.     

Refolding strategies for ketosteroid isomerase following insoluble expression in Escherichia coli

Dilution and column-based protein refolding techniques are compared for refolding Delta 5-3-ketosteroid isomerase (KSI) with a C-terminus his6-tag. Column refolding was performed by removing the denaturant while the protein was adsorbed in an immobilized metal affinity chromatography column. Both dilution refolding and a single-step column-based refolding strategy were optimized to maximize the recovery of KSI enzyme activity, and achieved refolding yields of 87% and 70% respectively. It was found that the column-based refolding yield was reduced at higher adsorbed protein concentrations. An elution gradient with increasing imidazole concentration was used to selectively elute the biologically active KSI protein following column refolding, with high molecular weight KSI aggregates retained in the column. An iterative column-refolding process was then developed to denature and refold protein retained in the column, which significantly increased the refolding yield at high-adsorbed protein concentrations. Repetition of the column refolding operation increased the refolding yield from 50% to 75% for protein adsorbed at a concentration of 2.9 mg/mL of adsorbent. Although for the KSI protein column-based refolding did not improve the overall refolding yield compared to dilution refolding, it may still be advantageous due to the ease of integration with purification operations, increased control over the refolding conditions, and the ability to segregate refolded protein from inactive aggregates during elution.     

Purification and refolding of human alpha5-subunit (PSMA5) of the 20S proteasome, expressed as inclusion bodies in Escherichia coli

The 20S proteasome is the central enzyme of nonlysosomal protein degradation in both the cytosol and nucleus. It is composed of 28 protein subunits which are arranged into four staggered heptameric rings. The outer rings consist of alpha-subunits which are responsible for binding of proteasome activators, inhibitors, and regulators. To better characterize human alpha5-subunit (PSMA5) of the 20S proteasome, we have established a high-efficiency Escherichia coli expression system. The DNA-coding sequence for the human PSMA5, which was subcloned into the vector pET-22b (+), has been expressed as inclusion bodies in E. coli BL21 (DE3). To produce the native PSMA5, straightforward protocols have been developed for refolding the human PSMA5 in the presence of surfactants using dilution refolding and size-exclusion chromatography matrix refolding methods. After refolding, recovery yields of about 20% were obtained, respectively, with purity above 95%. The human PSMA5 was detected by dynamic light scattering in refolding process, and the molecular weight of the final refolded product was measured using gel filtration chromatography, which indicates that the human PSMA5 exists mainly as tetramer.     

重组羧肽酶原B的复性方法研究

构建的羧肽酶原B表达质粒在大肠杆菌中获得高表达。但目的蛋白是以包涵体的形式存在。为了获得活性羧肽酶B,必须对其包涵体进行变复性。首先利用稀释复性确定了羧肽酶原B复性的最佳缓冲液;在凝胶过滤复性中,研究了柱长和洗脱流速对羧肽酶原B复性效率的影响;另外对比了稀释复性、透析复性、凝胶层析复性和Ni2 亲合层析法等四种方法对羧肽酶原B的复性效果。结果发现,这4种方法的复性效果有以下顺序:凝胶过滤复性>稀释复性>Ni2 亲合层析>透析复性。     

The effect of polyols on the reactivation of guanidium chloride-denatured arginine kinase from shrimp feneropenaeus chinensis muscle

The influence of glycerol, sorbitol, glucose and sucrose, on the refolding and reactivation courses of guanidine-denatured arginine kinase was studied. Glycerol, sucrose, and sorbitol, but not glucose, could improve the reactivation of the denatured arginine kinase, although in all cases aggregation was inhibited. Size exclusion chromatography showed that misfolded products were still formed during polyol-assisted refolding. The chemical and physical characteristics of polyols might explain the various observations.     

Unassisted refolding of urea-denatured arginine kinase from shrimp Feneropenaeus chinensis: evidence for two equilibrium intermediates in the refolding pathway

The refolding process and the equilibrium intermediates of urea-denatured arginine kinase (AK) were investigated by 1-anilino-8-naphthalenesulfonate (ANS) intrinsic fluorescence, far-UV circular dichroism (CD), size-exclusion chromatography (SEC), and enzymatic activity. In dilute denaturant, two equilibrium refolding intermediates (I and N') were discovered, and a refolding scheme of urea-denatured AK was proposed. During the refolding of urea-denatured AK, the fluorescence intensity increased remarkably, accompanied by a significant blue shift of the emission maximum and a pronounced increase in molar ellipticity of CD at 222 nm. The first folding intermediate (I) was inactive in urea solution ranging between 2.4 and 3.0 M. The second (N') existed between a 0.4- and 0.8-M urea solution, with slightly increased activity. Neither the blue shift emission maximum nor the molar ellipticity of CD at 222 nm showed significant changes in these two regions. The two intermediates were characterized by monitoring the ANS binding ability in various residual urea solutions, and two peaks of the emission intensity were observed in urea solutions of 0.6 and 2.8 M, respectively. The SEC results indicated that a distribution coefficient (K(D)) platform existed in urea solutions ranging between 2.4 and 3.0 M urea, suggesting that there was a similarly apparent protein profile and size in the urea solution region. The refolding kinetics showed that the urea-denatured AK was in two-phase refolding. Proline isomerization occurred in the unfolding process of AK, which blocked the slow phase of refolding. These results suggested that the refolding process of urea-denatured AK contained at the least two equilibrium refolding intermediates.     

A kinetic study of the folding of staphylococcal nuclease using size-exclusion chromatography.

The kinetics of the hydrodynamic volume change accompanying the reversible unfolding of staphylococcal nuclease have been observed by size-exclusion chromatography at 4 degrees C and pH 7.0 using the denaturant guanidine hydrochloride. The observed chromatographic profiles have been simulated by a six-component unfolding/refolding mechanism using a consistent set of equilibrium and kinetic parameters. The native protein is an equilibrium mixture of the cis and trans isomers of the peptide bond preceding proline-117. The native conformation containing the cis isomer dominates the equilibrium mixture, is more stable, and unfolds more slowly at its transition midpoint. The denatured protein is an equilibrium mixture of at least four components, the cis/trans isomers of proline-117 and one of the five remaining prolines. The dominant refolding pathway is initiated from the denatured component containing the trans isomer of proline-117. The six-component mechanism is consistent with tryptophan fluorescence kinetic measurements of the wild-type protein and with chromatographic measurements of a mutant P117G protein.