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。     

包涵体蛋白复性技术研究进展

本文对原核表达的包涵体蛋白的分离,洗涤,溶解及复性方法做了一个简单的总结。同时就国内外近几年的最新复性方法进行了概述。并分析了各种复性方法的利弊。     

重组包涵体蛋白质的折叠复性

综述了减少包涵体形成、包涵体分离和溶解以及包涵体折叠复性的策略及其最新进展 .详细讨论了包涵体蛋白质折叠复性的基本原则、包涵体折叠复性促进剂和包涵体折叠复性方法     

包涵体蛋白的层析复性技术研究进展

包涵体蛋白的复性是生物工程下游技术中的一个重要难题。层析法用于蛋白质复性是一种较新的、适用于大多数蛋白的方法。其原理是将层析技术应用于蛋白质复性和纯化,使变性蛋白质在层析柱上重折叠为正确的空间构象,在洗脱的同时实现部分纯化。本文详细介绍了蛋白质在5种层析柱上的复性方法、原理、应用及研究的新进展,为层析法对蛋白质复性的进一步应用提供依据。     

重组蛋白包涵体的复性研究

重组蛋白在大肠杆菌中的高表达往往形成不可溶、无生物活性的包涵体,需经过变性溶解后,在适当条件下复性形成天然的构象,才可恢复其生物活性．变复性实验是建立在对蛋白质体外折叠机制的了解的基础上．根据近年来对蛋白质折叠机制的认识和重组蛋白包涵体在复性方面的主要进展,论述以下3个方面的内容：1)蛋白质在细胞内的折叠机制;2)蛋白质体外折叠机制;3)蛋白质复性的策略和方法．     

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 。     

包含体内重组蛋白质的复性

具有临床、工业生产、药用功能的真核生物蛋白质的供给常常受到其天然来源的限制。可喜的是基因工程技术的发展使许多真核生物蛋白质能在细菌细胞中进行表达[1] 。大肠杆菌由于培养和基因操作容易而成为最受欢迎的表达系统 ,但是重组蛋白质在大肠杆菌中的高水平表达常常导致以包含体形式存在的胞內聚集的变性蛋白质的形成。这种变性蛋白质的量可高达总的重组蛋白质量的95%。由于以包含体形式存在的聚集蛋白质分子不具有正确的三维结构 (天然结构 ) ,它们在水溶液中通常不溶解且没有活性 ,因此大肠杆菌中包含体的形成就意味着可溶性重组蛋白…     

包涵体蛋白复性的几种方法

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。     

包含体蛋白质的复性研究进展

包含体的形成是异源蛋白质在大肠杆菌中高效表达的必然结果,也是目前产生重组蛋白质最有效的方法之一。不可溶、无生物活性的包含体必须经过变性、复性才能获得天然结构,完整特定的生物学功能。聚集是造成重组蛋白质复性产率低下的主要因素,因此理解蛋白质聚集机制,减少和防止聚集的发生是建立高效、高产率复性方法的关键。分子伴侣、低分子量添加物等在复性过程中的应用及新的复性方法的建立都大大提高了重组蛋白质复性产率。     

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。     

On-column refolding of an insoluble His6-tagged recombinant EC-SOD overexpressed in Escherichia coli

The EC-SOD cDNA was cloned by polymerase chain reaction (PCR) and inserted into the Escherichia coli expression plasmid pET-28a( ) and transformed into E. coli BL21 (DE3). The corresponding protein that was overexpressed as a recombinant His6-tagged EC-SOD was present in the form of inactive inclusion bodies. This structure was first solubilized under denaturant conditions (8.0 M urea). Then, after a capture step using immobilized metal affinity chromatography (IMAC), a gradual refolding of the protein was performed on-column using a linear urea gradient from 8.0 M to 1.5 M in the presence of glutathione (GSH) and oxidized glutathione (GSSG). The mass ratio of GSH to GSSG was 4:1. The purified enzyme was active,showing that at least part of the protein was properly refolded. The protein was made concentrated by ultrafiltration, and then isolated using Sephacryl S-200 HR. There were two protein peaks in the A280 profile.Based on the results of electrophoresis, we concluded that the two fractions were formed by protein subunits of the same mass, and in the fraction where the molecular weight was higher, the dimer was formed through the disulfide bond between subunits. Activities were detected in the two fractions, but the activity of the dimer was much higher than that of the single monomer. The special activities of the two fractions were found to be 3475 U/mg protein and 510 U/mg protein, respectively.     

Solid-phase refolding of poly-lysine tagged fusion protein of hEGF and angiogenin

A fusion protein, consisting of a human epidermal growth factor (hEGF) as the recognition domain and human angiogenin as the toxin domain, can be used as a targeted therapeutic against breast cancer cells among others. The fusion protein was expressed as inclusion body in recombinantE. coli, and when the conventional, solution-phase refolding process was used the refolding yield was very low due to severe aggregation. It was probably because of the opposite electric charge at a neutral pH resulting from the vastly different pI values of each domain. The solidphase refolding process that exploited the ionic interactions between ionic exchanger surface and the fusion protein was tried, but the adsorption yield was also very low, below 30%, regardless of the resins and pH conditions used. Therefore, to provide a higher ionic affinity toward the solid matrix, six lysine residues were tagged to theN-terminus of the hEGF domain. When heparin-Sepharose was used as the matrix, the adsorption capacity increased 2.5–3 times to about 88%. Besides the intrinsic affinity of angiogenin to heparin the poly-lysine tag provided additional ionic affinity. And the subsequent refolding yield increased nearly 13-fold, fromc.a 4.8% in the conventional refolding of the untagged fusion protein to 63.6%. The process was highly reproducible. The refolded protein in the column eluate retained R Nase bioactivity, of angiogenin.     

A simplified method for the efficient purification and refolding of recombinant human TRAIL

Tumor necrosis factor (TNF)-related apoptosis-inducing ligand (TRAIL) belongs to the TNF cytokine superfamily that specifically induces apoptosis in a broad spectrum of human cancer cell lines but not in most healthy cells. The antitumor potential of recombinant human TRAIL (rhTRAIL) has attracted great attention among biologists and oncologists. However, attempts to express rhTRAIL in Escherichia coli often results in limited yield of bioactive protein due to the formation of inclusion bodies (IBs), which are dense insoluble particulate protein aggregates inside cells. We describe herein a highly simplified method to produce pure bioactive rhTRAIL using E. coli. The method is straightforward and requires only basic laboratory equipment, with highly efficient purification and high yield of renaturation, and may also be applied to produce other proteins that form IBs in E. coli.     

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.     

Recombinant murine growth hormone from E. coli inclusion bodies: Expression,high‐pressure solubilization and refolding,and characterization of activity and structure

We expressed recombinant murine growth hormone (rmGH) in E. coli as a cost‐effective way to produce large quantities (gram scale) of the protein for use in murine studies of immunogenicity to therapeutic proteins. High hydrostatic pressure was used to achieve high solubility and high refolding yields of rmGH protein produced in E. coli inclusion bodies. A two‐step column purification protocol was used to produce 99% pure monomeric rmGH. Secondary and tertiary structures of purified rmGH were investigated using circular dichroism and 2D‐UV spectroscopy. The purified rmGH produced was found to be biologically active in hypophysectomized rats. © 2010 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Modeling of protein refolding from inclusion bodies

Overexpression of foreign proteins in Escherichia coli often leads to the formation of inclusion bodies （IBs）, which becomes the major bottleneck in the preparation of recombinant proteins and their applications. In the present study, 36 proteins from IBs were refolded using a simple refolding method. Refolding yields of these proteins were defined as the percentage of soluble pro- teins following dilution refoiding in the amount of denatured proteins in the samples before diluting into refolding buffer. Furthermore, a mathematical model was deduced to evaluate the role of biochemical proper- ties in the protein refolding. Our results indicated that under the experimental conditions, isoelectric point of proteins might be mostly contributing to the high effi- cacy of protein refolding since the increment of one unit resulted in a decrease of 14.83% in the refolding yield. Other important mediators were components of protein secondary structure and the molecular weight （R2= 0.98, P = 0.000, F-test）. Six proteins with low efficiency in the protein refolding possessed relatively low isoelectric points. Furthermore, refolding yields of six additional proteins from IBs were predicted and further validated by refolding the proteins under the same conditions. Therefore, the model of protein refold- ing developed here could be used to predict the refold- ing yields of proteins from IBs through a simple method. Our study will be suggestive to optimize the methods for protein refoiding from IBs according to their intrinsic properties.     

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.     

A novel system for continuous protein refolding and on-line capture by expanded bed adsorption

A novel two-step protein refolding strategy has been developed, where continuous renaturation-bydilution is followed by direct capture on an expanded bed adsorption (EBA) column. The performance of the overall process was tested on a N-terminally tagged version of human beta2-microglobulin (HAT-hbeta2m) both at analytical, small, and preparative scale. In a single scalable operation, extracted and denatured inclusion body proteins from Escherichia coli were continuously diluted into refolding buffer, using a short pipe reactor, allowing for a defined retention and refolding time, and then fed directly to an EBA column, where the protein was captured, washed, and finally eluted as soluble folded protein. Not only was the eluted protein in a correctly folded state, the purity of the HAThbeta2m was increased from 34% to 94%, and the product was concentrated sevenfold. The yield of the overall process was 45%, and the product loss was primarily a consequence of the refolding reaction rather than the EBA step. Full biological activity of HAT-hbeta2m was demonstrated after removal of the HAT-tag. In contrast to batch refolding, a continuous refolding strategy allows the conditions to be controlled and maintained throughout the process, irrespective of the batch size; i.e., it is readily scalable. Furthermore, the procedure is fast and tolerant toward aggregate formation, a common complication of in vitro protein refolding. In conclusion, this system represents a novel approach to small and preparative scale protein refolding, which should be applicable to many other proteins.     

Chaperone-mediated refolding of recombinant prochymosin

It has been verified that prochymosin is characterized by a two-stage refolding: dilution of unfolded protein into pH 11 buffer followed by neutralization at pH 8; the high-pH step is indispensable. Here we demonstrate that one-stage refolding around pH 8 can be achieved when GroE or 10-fold molar excess (rather than catalytic concentration) of protein disulfide isomerase (PDI) over prochymosin is present. The helping effect varies with the oxidation states of prochymosin. GroE and PDI increase the reactivation of the unfolded, partially reduced and the unfolded, oxidized prochymosin from 5% to 40% and from 50% to 100%, respectively. For the unfolded and fully reduced prochymosin, GroE does not have a positive effect, whereas PDI promotes renaturation from 2% to 28%. Based on our previous and present observations, we propose that at pH 8 there may be two kinds of incorrect interactions within and between prochymosin polypeptides leading to unproductive pathways: one prevents disulfide rearrangement, which can be avoided by high pH; the other interferes with acquisition of native conformation, which can be relieved by GroE and PDI.