In situ protein folding and activation in bacterial inclusion bodies

Recent observations indicate that bacterial inclusion bodies formed in absence of the main chaperone DnaK result largely enriched in functional, properly folded recombinant proteins. Unfortunately, the molecular basis of this intriguing fact, with obvious biotechnological interest, remains unsolved. We have explored here two non-excluding physiological mechanisms that could account for this observation, namely selective removal of inactive polypeptides from inclusion bodies or in situ functional activation of the embedded proteins. By combining structural and functional analysis, we have not observed any preferential selection of inactive and misfolded protein species by the dissagregating machinery during inclusion body disintegration. Instead, our data strongly support that folding intermediates aggregated as inclusion bodies could complete their natural folding process once deposited in protein clusters, which conduces to significant functional activation. In addition, in situ folding and protein activation in inclusion bodies is negatively regulated by the chaperone DnaK.     

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.     

Techno-economic evaluation of an inclusion body solubilization and recombinant protein refolding process

Expression of recombinant proteins in Escherichia coli is normally accompanied by the formation of inclusion bodies (IBs). To obtain the protein product in an active (native) soluble form, the IBs must be first solubilized, and thereafter, the soluble, often denatured and reduced protein must be refolded. Several technically feasible alternatives to conduct IBs solubilization and on-column refolding have been proposed in recent years. However, rarely these on-column refolding alternatives have been evaluated from an economical point of view, questioning the feasibility of their implementation at a preparative scale. The presented study assesses the economic performance of four distinct process alternatives that include pH induced IBs solubilization and protein refolding (pH_IndSR); IBs solubilization using urea, dithiothreitol (DTT), and alkaline pH followed by batch size-exclusion protein refolding; inclusion bodies (IBs) solubilization using urea, DTT, and alkaline pH followed by simulated moving bed (SMB) size-exclusion protein refolding, and IBs solubilization using urea, DTT and alkaline pH followed by batch dilution protein refolding. The economic performance was judged on the basis of the direct fixed capital, and the production cost per unit of product (P(C)). This work shows that (1) pH_IndSR system is a relatively economical process, because of the low IBs solubilization cost; (2) substituting β-mercaptoethanol for dithiothreithol is an attractive alternative, as it significantly decreases the product cost contribution from the IBs solubilization; and (3) protein refolding by size-exclusion chromatography becomes economically attractive by changing the mode of operation of the chromatographic reactor from batch to continuous using SMB technology.     

TRAIL包涵体在细胞内重折叠现象的初步研究

肿瘤坏死因子相关凋亡诱导配体（Ap02L／TRAIL）是一种新型的抗肿瘤蛋白。但在大肠杆菌表达系统中,表达的TRAIL蛋白往往容易聚集形成包涵体。本文对重组TRAIL包涵体在胞内重折叠转化成可溶性TRAIL蛋白作了初步探索,结果表明：当蛋白表达后,迅速降低温度至30℃并添加50μg／mL氯霉素继续培养4h,可溶性TRAIL产量可提高至16．7％。这一结果在3．7L罐上也得到了证实,可溶性TRAIL表达量达到14．5％。     

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     

Extraction of rIL-2 inclusion bodies from Escherichia coli using cross-flow filtration

A cross-flow membrane filtration process was developed for the recovery of rIL-2 inclusion bodies from homogenized Escherichia coli. The membrane extraction process was comprised of a two-step diafiltration followed by an extraction with 7 M GuHCl and a 40-fold dilution of the solubilized inclusion bodies into 0.01 M Tris-HCl, 0.035 M NaCl, pH 7.9. The first diafiltration was with a 0.03 M Tris-HCl, 5 mM ethylenediaminetetraacetic acid (EDTA), pH 8, followed by a diafiltration with 1.75 M GuHCl. All of the insoluble rIL-2 was retained behind the membrane, whereas a GuHCl wash solubilized approximately 15% of the rIL-2. The membrane process increased the yield of rIL-2 in the diluted extract by threefold as compared to a similar centrifuge process with a significant increase in purity as determined by reverse-phase high-performance liquid chromatography (HPLC). (c) 1994 John Wiley & Sons, Inc.     

Chemical treatment of Escherichia coli: 3. Selective extraction of a recombinant protein from cytoplasmic inclusion bodies in intact cells

In previous parts of this study we developed procedures for the high‐efficiency chemical extraction of soluble and insoluble protein from intact Escherichia coli cells. Although high yields were obtained, extraction of recombinant protein directly from cytoplasmic inclusion bodies led to low product purity due to coextraction of soluble contaminants. In this work, a two‐stage procedure for the selective extraction of recombinant protein at high efficiency and high purity is reported. In the first stage, inclusion‐body stability is promoted by the addition of 15 mM 2‐hydroxyethyldisulfide (2‐HEDS), also known as oxidized β‐mercaptoethanol, to the permeabilization buffer (6 M urea + 3 mM ethylenediaminetetraacetate [EDTA]). 2‐HEDS is an oxidizing agent believed to promote disulfide bond formation, rendering the inclusion body resistant to solubilization in 6 M urea. Contaminating proteins are separated from the inclusion‐body fraction by centrifugation. In the second stage, disulfide bonds are readily eliminated by including reducing agent (20 mM dithiothreitol [DTT]) into the permeabilization buffer. Extraction using this selective two‐stage process yielded an 81% (w/w) recovery of the recombinant protein Long‐R³‐IGF‐I from inclusion bodies located in the cytoplasm of intact E. coli, at a purity of 46% (w/w). This was comparable to that achieved by conventional extraction (mechanical disruption followed by centrifugation and solubilization). A pilot‐scale procedure was also demonstrated using a stirred reactor and diafiltration. This is the first reported study that achieves both high extraction efficiency and selectivity by the chemical treatment of cytoplasmic inclusion bodies in intact bacterial cells. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 62: 455–460, 1999.     

Purification and on-column refolding of EGFP overexpressed as inclusion bodies in Escherichia coli with expanded bed anion exchange chromatography

The enhanced green fluorescent protein (EGFP) was over-expressed in Escherichia coli as inclusion bodies to increase its quantity and to facilitate its purification. Insoluble EGFP has been purified on Q Hyper Z matrix by expanded bed adsorption after solubilization in 8 M urea. The adsorption was made in expanded bed mode to avoid centrifugation. EBA-column refolding was done by elimination of urea and elution with NaCl. The EGFP was obtained as a highly purified soluble form with similar behavior in fluorescence and electrophoresis as native EGFP.     

茂原链轮丝菌转谷氨酰胺酶基因在大肠杆菌中高效表达

利用PCR方法从茂原链轮丝菌(Streptoverticillium mobaraense)基因组DNA扩增出微生物转谷氨酰胺酶(Microbial Transglutaminase,MTG)的基因片段,并构建表达质粒Pet-MTG。后者在大肠杆菌（Rosetta DE3）中得到高效表达,但表达的MTG存在于包涵体中。经洗涤、变性和复性,并以强阳离子交换层析纯化,获得了SDS-PAGE纯的MTG,并具有与天然酶几乎相同的比活性。此项工作为工业化生产MTG打下了基础。     

New tools for recombinant protein production in Escherichia coli: A 5‐year update

The production of proteins in sufficient amounts is key for their study or use as biotherapeutic agents. Escherichia coli is the host of choice for recombinant protein production given its fast growth, easy manipulation, and cost‐effectiveness. As such, its protein production capabilities are continuously being improved. Also, the associated tools (such as plasmids and cultivation conditions) are subject of ongoing research to optimize product yield. In this work, we review the latest advances in recombinant protein production in E. coli.     

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.     

Streptomyces hygroscopicus谷氨酰胺转胺酶酶原基因的鉴定及在大肠杆菌中的表达

[目的]鉴定来源于吸水链霉菌的谷氨酰胺转胺酶基因;研究其在大肠杆菌系统的克隆与表达;分析该酶与其同源酶的活性中心氨基酸序列.[方法]从本实验室筛选的吸水链霉菌(Streptomyces hygroscopicus;CCTCC M203062)发酵液中,分离纯化得到谷氨酰胺转胺酶酶原(pro-MTGase),测得N-端前十个氨基酸序列并与其它链霉菌来源的相应基因序列比较设计引物,扩增得到pro-MTGase 基因,将该基因插入到表达载体pET-20b( )信号肽pelB下游,构建分泌型表达载体pET/pro-MTG,并转化不同的大肠杆菌宿主BL21(DE3)和Rosetta(DE3)pLysS.[结果]获得了pro-MTGase的完整基因序列,多重碱基序列比对表明其与S.platensis和S.caniferus的pro-MTGase基因同源性高达92%.利用Rosetta(DE3)pLysS通过降温至24℃诱导策略,获得部分胞外表达的酶原.SDS-PAGE显示,胞外表达重组蛋白的分子量约为44kDa,与吸水链霉菌表达的天然酶原相符.诱导4 h后发酵液中的重组酶原经胰蛋白酶活化为成熟酶后测得最高酶活为0.24U/mL.[结论]该研究是对吸水链霉菌的谷氨酰胺转胺酶基因的首次报道,也是国内首次利用大肠杆菌实现pro-MTGase的胞外可溶性表达.     

Refolding strategies from inclusion bodies in a structural genomics project

The South-Paris Yeast Structural Genomics Project aims at systematically expressing, purifying and determining the structure of S. cerevisiae proteins with no detectable homology to proteins of known structure. We brought 250 yeast ORFs to expression in E. coli, but 37% of them form inclusion bodies. This important fraction of proteins that are well expressed but lost for structural studies prompted us to test methodologies to recover these proteins. Three different strategies were explored in parallel on a set of 20 proteins: (1) refolding from solubilized inclusion bodies using an original and fast 96-well plates screening test, (2) co-expression of the targets in E. coli with DnaK-DnaJ-GrpE and GroEL-GroES chaperones, and (3) use of the cell-free expression system. Most of the tested proteins (17/20) could be resolubilized at least by one approach, but the subsequent purification proved to be difficult for most of them.     

Prediction of protein solubility in Escherichia coli using logistic regression

In this article we present a new and more accurate model for the prediction of the solubility of proteins overexpressed in the bacterium Escherichia coli. The model uses the statistical technique of logistic regression. To build this model, 32 parameters that could potentially correlate well with solubility were used. In addition, the protein database was expanded compared to those used previously. We tested several different implementations of logistic regression with varied results. The best implementation, which is the one we report, exhibits excellent overall prediction accuracies: 94% for the model and 87% by cross‐validation. For comparison, we also tested discriminant analysis using the same parameters, and we obtained a less accurate prediction (69% cross‐validation accuracy for the stepwise forward plus interactions model). Biotechnol. Bioeng. 2010; 105: 374–383. © 2009 Wiley Periodicals, Inc.     

Folding and aggregation of TEM beta-lactamase: analogies with the formation of inclusion bodies in Escherichia coli.

The enzyme TEM beta-lactamase has been used as a model for understanding the pathway leading to formation of inclusion bodies in Escherichia coli. The equilibrium denaturation of TEM beta-lactamase revealed that an intermediate that has lost enzymatic activity, native protein fluorescence, and UV absorption, but retains 60% of the native circular dichroism signal, becomes populated at intermediate (1.0-1.4 M) concentrations of guanidium chloride (GdmCl). This species exhibits a large increase in bis-1-anilino-8-naphthalene sulfonic acid fluorescence, indicating the presence of exposed hydrophobic surfaces. When TEM beta-lactamase was unfolded in different initial concentrations of GdmCl and refolded to the same final conditions by dialysis a distinct minimum in the yield of active protein was observed for initial concentrations of GdmCl in the 1.0-1.5 M range. It was shown that the lower reactivation yield was solely due to the formation of noncovalently linked aggregates. We propose that the aggregation of TEM beta-lactamase involves the association of a compact state having partially exposed hydrophobic surfaces. This hypothesis is consistent with our recent findings that TEM beta-lactamase inclusion bodies contains extensive secondary structure (Przybycien TM, Dunn JP, Valax P, Georgiou G, 1994, Protein Eng 7:131-136). Finally, we have also shown that protein aggregation was enhanced at higher temperatures and in the presence of 5 mM dithiothreitol and was inhibited by the addition of sucrose. These conditions exert a similar effect on the formation of inclusion bodies in vivo.     

Production of soluble and active microbial transglutaminase in Escherichia coli for site‐specific antibody drug conjugation

Applications of microbial transglutaminase (mTGase) produced from Streptomyces mobarensis (S. mobarensis) were recently extended from food to pharmaceutical industry. To use mTGase for clinical applications, like generation of site specific antibody drug conjugates, it would be beneficial to manufacture mTGase in Escherichia coli (E. coli). To date, attempts to express recombinant soluble and active S. mobarensis mTGase have been largely unsuccessful. mTGase from S. mobarensis is naturally expressed as proenzyme and stepwise proteolytically processed into its active mature form outside of the bacterial cell. The pro‐domain is essential for correct folding of mTGase as well as for inhibiting activity of mTGase inside the cell. Here, we report a genetically modified mTGase that has full activity and can be expressed at high yields in the cytoplasm of E. coli. To achieve this we performed an alanine‐scan of the mTGase pro‐domain and identified mutants that maintain its chaperone function but destabilize the cleaved pro‐domain/mTGase interaction in a temperature dependent fashion. This allows proper folding of mTGase and keeps the enzyme inactive during expression at 20°C, but results in full activity when shifted to 37°C due to loosen domain interactions. The insertion of the 3C protease cleavage site together with pro‐domain alanine mutants Tyr14, Ile24, or Asn25 facilitate high yields (30–75 mg/L), and produced an enzyme with activity identical to wild type mTGase from S. mobarensis. Site‐specific antibody drug conjugates made with the E .coli produced mTGase demonstrated identical potency in an in vitro cell assay to those made with mTGase from S. mobarensis.     

On-column refolding and purification of transglutaminase from Streptomyces fradiae expressed as inclusion bodies in Escherichia coli

Since transglutaminase (TGase) have been widely used in industry, mass production of the enzyme is especially necessary. The mature TGase gene from Streptomyces fradiae was cloned into pET21a and overexpressed in Escherichia coli BL21(DE3). The recombinant TGase was formed as inclusion bodies, and its content was as high as 55% of the total protein content. The insoluble fractions were separated from cellular debris by centrifugation and solubilized with 8 M urea. With an on-column refolding procedure based on cation SP Fast Flow chromatography with dual-gradient, the active TGase protein was recovered efficiently from inclusion bodies. The final purified product was 95% pure detected by SDS-PAGE. Under appropriate experimental conditions, the protein yield and specific activity of the TGase were up to 53% and 21 U/mg, respectively. Furthermore, the refolded recombinant protein demonstrated nearly identical ability to polymerized BSA compared with that of native TGase. One hundred and five milligrams of refolded TGase protein was obtained from 3.2g wet weight cells in the 400 ml cell culture.     

Real time detection and quantification of inclusion bodies expressed in Escherichia coli by impedance measurements

Escherichia coli expressing human growth hormone as inclusion bodies was cultured in a fermenter. Real time, non-invasive detection and quantification of inclusion body protein expressed in E. coli was performed by impedance measurements at 50 MHz and 180 MHz. At 50 MHz rotation of dipoles of the protein and their proton fluctuation, i.e., -dispersion of protein aggregates formed inside the cell as a result of expressed protein, results in an additional decrease in impedance. At 180 MHz the impedance remained at a plateau. In a high cell density E. coli culture, after induction with IPTG, when the cell mass remained unchanged, an increase in the magnitude of -dispersion was observed at 50 MHz. This was due to the formation and subsequent increase in the concentration of r-human growth hormone which aggregate as inclusion bodies. The estimation of inclusion bodies by taking the ratio of impedance at 180 MHz and at 50 Mhz matched with the amount of protein estimated after extraction and purification (coefficient of correlation was 0.92). This is the first report of real time detection and monitoring of recombinant protein expressed as inclusion bodies by impedance measurements.     

大肠杆菌高效表达重组蛋白策略

大肠杆菌表达系统是基因表达技术中发展最早和目前应用最广的经典表达系统。利用该系统表达重组蛋白具有许多优越性,但其表达效率受诸多因素的影响。本文综述国内外利用大肠杆菌表达系统高效表达外源蛋白的策略,主要包括选择合适的启动子、改变信号肽结构、提高mRNA稳定性、提高翻译效率、表达稀有密码子、降低包涵体形成及蛋白降解,利用融合蛋白与分子伴侣、调控发酵条件实现高密度培养等。