包涵体蛋白体外复性的研究进展

外源基因在大肠杆菌中高水平表达时 ,通常会形成无活性的蛋白聚集体即包涵体。包涵体富含表达的重组蛋白 ,经分离、变性溶解后须再经过一个合适的复性过程实现变性蛋白的重折叠 ,才能够得到生物活性蛋白。近年来 ,发展了许多特异的策略和方法来从包涵体中复性重组蛋白。最近的进展包括固定化复性以及用一些低分子量的添加剂等来减少复性过程中蛋白质的聚集 ,提高活性蛋白的产率。     

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.     

Protein folding in vivo and renaturation of recombinant proteins from inclusion bodies

Eukaryotic proteins expressed inEscherichia coli often accumulate within the cell as insoluble protein aggregates or inclusion bodies. The recovery of structure and activity from inclusion bodies is a complex process, there are no general rules for efficient renaturation. Research into understanding how proteins fold in vivo is giving rise to potentially new refolding methods, for example, using molecular chaperones. In this article we review what is understood about the main three classes of chaperone: the Stress 60, Stress 70, and Stress 90 proteins. We also give an overview of current process strategies for renaturing inclusion bodies, and report the use of novel developments that have enhanced refolding yields.     

A method for increasing the yield of properly folded recombinant fusion proteins: single-chain immunotoxins from renaturation of bacterial inclusion bodies.

Many proteins produced in Escherichia coli accumulate in inclusion bodies. We have systematically evaluated the parameters that affect the refolding and renaturation of enzymatically active molecules from bacterial inclusion bodies containing a recombinant single-chain immunotoxin, B3(Fv)-PE38KDEL. This recombinant molecule is composed of the variable domains of monoclonal antibody B3 (B3(Fv)) fused to a truncated mutant form of Pseudomonas exotoxin A (PE38KDEL). This immunotoxin kills carcinoma cells in vitro, causes tumor regression in animal tumor models, and is being developed as an anti-cancer therapeutic agent (Brinkmann et al., 1991, Proc. Natl. Acad. Sci. USA 88, 8616-8620). Like many other recombinant proteins, B3(Fv)-PE38KDEL is produced in E. coli in inclusion bodies and must be denatured and refolded to become active. This requires correct folding, formation of native disulfide bonds, and the association of different domains. All these steps are strongly dependent on the renaturation conditions used. Optimum conditions of refolding were obtained by the addition of reduced and oxidized thiol reagents to promote disulfide bond formation and the addition of a labilizing agent such as L-arginine. Furthermore, the necessity to reactivate proteins at low protein concentrations due to its tendency to aggregate at high concentrations was overcome by a step-by-step addition of denatured and reduced protein into the refolding solution. This approach should be useful for the production of active forms of other recombinant proteins.     

蛋白质复性研究进展

许多蛋白在大肠杆菌中高效表达时,其产物常以无活性的包含体形式存在,包含体蛋白的复性往往是制备这些蛋白的关键步骤之一,蛋白复性包括肽链折叠和分子内二硫键的氧化这两个互相影响的过程,本文综述了蛋白折叠过程的研究进展,及促进蛋白折叠和二硫键氧化的方法。     

液胶色谱柱复性在低分子量尿激酶原突变体（DscuPA—32K）中的应用

将构建一种具溶栓和抗栓以重功能尿激酶原突变体（DscuPA-32K)基因,在大肠杆菌中进行表达。由于DscuPA-32K分子较大并且表达量较高,目的的性质基本以包涵体的形式存在。包涵体中的蛋白质是无活性的蛋白质,为了获得有活性的蛋白质,就需要对包涵体进行变性及复性。尝试了一种新的凝胶色谱柱复性方法,并通过柱复性方法与常规的稀释复性方法进行了比较,发现柱复性方法明显优于稀释复性方法,具有成本低,效率高,并对目的的蛋白质（DscuPA-32K)进行了初步纯化等优点,尤其对酶这一类容易失活降解的蛋白质进行复性时,很值得进行推广应用。     

包涵体复性研究进展(英文)

用基因工程技术在大肠杆菌高水平表达重组蛋白时,通常形成无生物活性的包涵体。包涵体在体外经分离、溶解与重折叠后可实现复性,表现为具有生物活性的蛋白。总结了包涵体的相关复性技术,重点介绍重折叠的最新进展情况 。     

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%.     

Technical refolding of proteins: Do we have freedom to operate?

Expression as inclusion bodies in Escherichia coli is a widely used method for the large-scale production of therapeutic proteins that do not require post-translational modifications. High expression yields and simple recovery steps of inclusion bodies from the host cells are attractive features industrially. However, the value of an inclusion body-based process is dominated by the solubilization and refolding technologies. Scale-invariant technologies that are economical and applicable for a wide range of proteins are requested by industry. The main challenge is to convert the denatured protein into its native conformation at high yields. Refolding competes with misfolding and aggregation. Thus, the yield of native monomer depends strongly on the initial protein concentrations in the refolding solution. Reasonable yields are attained at low concentrations (≤0.1 mg/mL). However, large buffer tanks and time-consuming concentration steps are required. We attempt to answer the question of the extent to which refolding of proteins is protected by patents. Low-molecular mass additives have been developed to improve refolding yields through the stabilization of the protein in solution and shielding hydrophobic patches. Progress has been made in the field of high-pressure renaturation and on-column refolding. Mixing times of the denatured protein in the refolding buffer have been reduced using newly developed devices and the introduction of specific mixers. Concepts of continuous refolding have been introduced to reduce tank sizes and increase yields. Some of the patents covering refolding of proteins will soon expire or have already expired. This gives more freedom to operate.     

An Automatic Refolding Apparatus for Preparative-Scale Protein Production

Protein refolding is an important process to recover active recombinant proteins from inclusion bodies. Refolding by simple dilution, dialysis and on-column refolding methods are the most common techniques reported in the literature. However, the refolding process is time-consuming and laborious due to the variability of the behavior of each protein and requires a great deal of trial-and-error to achieve success. Hence, there is a need for automation to make the whole process as convenient as possible. In this study, we invented an automatic apparatus that integrated three refolding techniques: varying dilution, dialysis and on-column refolding. We demonstrated the effectiveness of this technology by varying the flow rates of the dilution buffer into the denatured protein and testing different refolding methods. We carried out different refolding methods on this apparatus: a combination of dilution and dialysis for human stromal cell-derived factor 1 (SDF-1/CXCL12) and thioredoxin fused-human artemin protein (Trx-ARTN); dilution refolding for thioredoxin fused-human insulin-like growth factor I protein (Trx-IGF1) and enhanced fluorescent protein (EGFP); and on-column refolding for bovine serum albumin (BSA). The protein refolding processes of these five proteins were preliminarily optimized using the slowly descending denaturants (or additives) method. Using this strategy of decreasing denaturants concentration, the efficiency of protein refolding was found to produce higher quantities of native protein. The standard refolding apparatus configuration can support different operations for different applications; it is not limited to simple dilution, dialysis and on-column refolding techniques. Refolding by slowly decreasing denaturants concentration, followed by concentration or purification on-column, may be a useful strategy for rapid and efficient recovery of active proteins from inclusion bodies. An automatic refolding apparatus employing this flexible strategy may provide a powerful tool for preparative scale protein production.     

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。     

Direct refolding of inclusion bodies using reversed micelles

The protein refolding of inclusion bodies was investigated using reversed micelles formed by aerosol OT (AOT). Ribonuclease A (RNase A) was overexpressed in Escherichia coli and used as native inclusion bodies. The enzymatic activity of RNase A was completely regained from the inclusion bodies within 14 h by solubilization in reversed micelles. To further enhance the refolding rate, a molecular chaperone, GroEL, was incorporated into the refolding system. The resultant refolding system including GroEL showed better performance under optimized conditions for the refolding of RNase A inclusion bodies. The refolding rate was considerably improved by the addition of the molecular chaperone, and the refolding step was completed in 1 h. The protein refolding in the GroEL-containing refolding system was strongly dependent on the coexistence of ATP and Mg2+, suggesting that the GroEL hosted in the reversed micelles was biologically active and assisted in the renaturation of the inclusion bodies. The addition of cold acetone to the reversed micellar solution allowed over 90% recovery of the renatured RNase A.     

High recovery of prochymosin from inclusion bodies using controlled air oxidation

Refolding of proteins from inclusion bodies is a field of increasing interest for obtaining large amounts of active enzymes. Consequently, the development of inexpensive and scalable processes is required. This is particularly challenging in the case of eukaryotic proteins containing cysteines, which may form disulfide bonds in the native active protein. Previous studies have shown that the formation of disulfide bonds is essential for the refolding of prochymosin. In this work we demonstrate that air oxidation can be efficiently used for the refolding of prochymosin and that 48% of the unfolded protein can be recovered as active enzyme at a final protein concentration of 0.8 mg/ml. Refolding of the protein strictly correlates with the change in pH of the refolding solution. We were able to follow the degree of oxidative renaturation of the prochymosin by simply measuring pH. Thus, the scaling up of the refolding system under controlled conditions was easily achieved. Analyses of different substances as folding aids indicate that the use of L-arginine or neutral surfactants improves the recovery of active protein up to 67% of the initial protein. The overall results indicate that prochymosin can be efficiently and inexpensively refolded with high yields by controlled air oxidation.     

Confronting high-throughput protein refolding using high pressure and solution screens

Over-expression of heterologous proteins in Escherichia coli is commonly hindered by the formation of inclusion bodies. Nevertheless, refolding of proteins in vitro has become an essential requirement in the development of structural genomics (proteomics) and as a means of recovering functional proteins from inclusion bodies. Many distinct methods for protein refolding are now in use. However, regardless of method used, developing a reliable protein refolding protocol still requires significant optimization through trial and error. Many proteins fall into the category of "Challenging" or "Difficult to Express" and are problematic to refold using traditional chaotrope-based refolding techniques. This review discusses new methods for improving protein refolding, such as implementing high hydrostatic pressure, using small molecule additives to enhance traditional protein refolding strategies, as well as developing practical methods for performing refolding studies to maximize their reliability and utility. The strategies examined here focus on high-throughput, automated refolding screens, which can be applied to structural genomic projects.     

Effect of chemical chaperones in improving the solubility of recombinant proteins in Escherichia coli

The recovery of active proteins from inclusion bodies usually involves chaotrope-induced denaturation, followed by refolding of the unfolded protein. The efficiency of renaturation is low, leading to reduced yield of the final product. In this work, we report that recombinant proteins can be overexpressed in the soluble form in the host expression system by incorporating compatible solutes during protein expression. Green fluorescent protein (GFP), which was otherwise expressed as inclusion bodies, could be made to partition off into the soluble fraction when sorbitol and arginine, but not ethylene glycol, were present in the growth medium. Arginine and sorbitol increased the production of soluble protein, while ethylene glycol did not. Production of ATP increased in the presence of sorbitol and arginine, but not ethylene glycol. A control experiment with fructose addition indicated that protein solubilization was not due to a simple ATP increase. We have successfully reproduced these results with the N-terminal domain of HypF (HypF-N), a bacterial protein which forms inclusion bodies in Escherichia coli. Instead of forming inclusion bodies, HypF-N could be expressed as a soluble protein in the presence of sorbitol, arginine, and trehalose in the expression medium.     

Isolation, renaturation, and formation of disulfide bonds of eukaryotic proteins expressed in Escherichia coli as inclusion bodies

Expression of recombinant proteins in Escherichia coli often results in the formation of insoluble inclusion bodies, In case of expression of eukaryotic proteins containing cysteine, which may form disulfide bonds in the native active protein, often nonnative inter- and intramolecular disulfide bonds exist in the inclusion bodies. Hence, several methods have been developed to isolate recombinant eukaryotic polypeptides from inclusion bodies, and to generate native disulfide bonds, to get active proteins. This article summarizes the different steps and methods of isolation and renaturation of eukaryotic proteins containing disulfide bonds, which have been expressed in E. coli as inclusion bodies, and shows which methods originally developed for studying the folding mechanism of naturally occurring proteins have been successfully adapted for reactivation of recombinant eukaryotic proteins. (c) 1993 John Wiley & Sons, Inc.     

Refolding and simultaneous purification by three-phase partitioning of recombinant proteins from inclusion bodies

Many recombinant eukaryotic proteins tend to form insoluble aggregates called inclusion bodies, especially when expressed in Escherichia coli. We report the first application of the technique of three-phase partitioning (TPP) to obtain correctly refolded active proteins from solubilized inclusion bodies. TPP was used for refolding 12 different proteins overexpressed in E. coli. In each case, the protein refolded by TPP gave either higher refolding yield than the earlier reported method or succeeded where earlier efforts have failed. TPP-refolded proteins were characterized and compared to conventionally purified proteins in terms of their spectral characteristics and/or biological activity. The methodology is scaleable and parallelizable and does not require subsequent concentration steps. This approach may serve as a useful complement to existing refolding strategies of diverse proteins from inclusion bodies.     

重组N-乙酰鸟氨酸脱乙酰基酶的表达、纯化和复性研究

报道重组N-乙酰鸟氨酸脱乙酰基酶(NAOase)的研究进展。重组NAOase由大肠杆菌argE基因编码,在重组菌BL21(DE3)-pET22b-argE中的表达量为32.5%,大多以无活性的包涵体存在。低温诱导可增大有活性的可溶表达部分的比例。可溶性NAOase经Ni-NTA凝胶亲和纯化后得到SDS-PAGE电泳纯的酶,比酶活为1193.2u/mg蛋白。诱导条件影响整菌蛋白的成分及比例。37℃诱导生成的包涵体经尿素梯度洗涤后纯度较22℃高。低的蛋白浓度和合适的氧化还原体系是影响复性的关键因素。稀释法和透析法皆可使包涵体部分复性。在合适的条件下以稀释法复性时,约有17.78%包涵体可顺利复活。包涵体经尿素洗涤、溶解、Ni-NTA凝胶柱亲和纯化后,获得了高纯度的NAOase。     

L-cysteine-enhanced renaturation of bioactive soluble tumor necrosis factor ligand family member LIGHT from inclusion bodies in Escherichia coli

LIGHT is a membrane-bound protein that belongs to the tumor necrosis factor (TNF) superfamily ligands. In this study, we established an effective strategy for producing a bioactive soluble form of LIGHT (sLIGHT), an extracellular region (Ile??-Val2??) of human LIGHT. Because sLIGHT was expressed as inclusion bodies in Escherichia coli, we investigated reagents that enhance the renaturation of sLIGHT from the inclusion bodies. Interestingly, L-cysteine in the denaturation buffer containing 3.5 M guanidine hydrochloride significantly improved the renaturation efficiency of sLIGHT. The effect of L-cysteine was synergistically enhanced by L-arginine in the refolding buffer. The optimal concentrations of L-cysteine and L-arginine in the denaturation and refolding buffers were 8 mM and 0.8 M, respectively. With these buffers, approximately 90 mg of sLIGHT was purified from 200 g of frozen E. coli cells. sLIGHT thus obtained significantly induced apoptosis in the WiDr human colon adenocarcinoma cell line at nanomolar concentrations, the same amount of sLIGHT that was produced by Sf9 insect cells. These results suggest that L-cysteine in the denaturation buffer enhances the renaturation of recombinant proteins from inclusion bodies in E. coli.     

Estimating the potential refolding yield of recombinant proteins expressed as inclusion bodies

Recombinant protein production in bacteria is efficient except that insoluble inclusion bodies form when some gene sequences are expressed. Such proteins must undergo renaturation, which is an inefficient process due to protein aggregation on dilution from concentrated denaturant. In this study, the protein-protein interactions of eight distinct inclusion-body proteins are quantified, in different solution conditions, by measurement of protein second virial coefficients (SVCs). Protein solubility is shown to decrease as the SVC is reduced (i.e., as protein interactions become more attractive). Plots of SVC versus denaturant concentration demonstrate two clear groupings of proteins: a more aggregative group and a group having higher SVC and better solubility. A correlation of the measured SVC with protein molecular weight and hydropathicity, that is able to predict which group each of the eight proteins falls into, is presented. The inclusion of additives known to inhibit aggregation during renaturation improves solubility and increases the SVC of both protein groups. Furthermore, an estimate of maximum refolding yield (or solubility) using high-performance liquid chromatography was obtained for each protein tested, under different environmental conditions, enabling a relationship between "yield" and SVC to be demonstrated. Combined, the results enable an approximate estimation of the maximum refolding yield that is attainable for each of the eight proteins examined, under a selected chemical environment. Although the correlations must be tested with a far larger set of protein sequences, this work represents a significant move beyond empirical approaches for optimizing renaturation conditions. The approach moves toward the ideal of predicting maximum refolding yield using simple bioinformatic metrics that can be estimated from the gene sequence. Such a capability could potentially "screen," in silico, those sequences suitable for expression in bacteria from those that must be expressed in more complex hosts.