A New <Emphasis Type="Italic">Escherichia coli</Emphasis> Strain Producing Human Tumor Necrosis Factor

An Escherichia coli strain producing human tumor necrosis factor (TNF-α) was obtained using a semisynthetic gene partially optimized in respect of codon composition and a phage T7 promoter. The expression product was accumulated in cells as inclusion bodies in a yield of 50–70 mg/l of culture medium. The recombinant TNF-α in the form of inclusion bodies was used for immunization of rats to give a polyclonal antiserum. The resulting antibodies were specific under the immunoblotting conditions to the antigen used for the immunization. A dilution-based refolding procedure was developed; it provided a yield of soluble protein exceeding 85%.     

Overexpression, effective renaturation, and bioactivity of novel single-chain antibodies against TNF-alpha

Neutralization of tumor necrosis factor-alpha (TNF-alpha) has become an effective therapeutic strategy for TNF-related autoimmune diseases. Due to the limitations of the large molecular inhibitors in the therapy, development of novel TNF-alpha inhibitors is very attractive and useful. In this study, based on the previously designed domain antibody, two novel human anti-TNF single-chain antibodies were constructed using modular consensus frameworks of human antibody as scaffold to display the antagonistic peptides. A variety of expression plasmids were used to determine the optimal expression system. The single-chain antibodies were always overexpressed in E.coli BL21(DE3) host as inclusion bodies. Under the optimized refolding conditions, the inclusion bodies were renatured successfully and the refolded single-chain antibodies could bind with TNF-alpha and block TNF-induced cytotoxicity on L929 cells. The bioactivity of the single-chain antibodies was significantly increased over the domain antibody.     

Optimization of inclusion body solubilization and renaturation of recombinant human growth hormone from Escherichia coli

Recombinant human growth hormone (r-hGH) was expressed in Escherichia coli as inclusion bodies. In 10 h of fed-batch fermentation, 1.6 g/L of r-hGH was produced at a cell concentration of 25 g dry cell weight/L. Inclusion bodies from the cells were isolated and purified to homogeneity. Various buffers with and without reducing agents were used to solubilize r-hGH from the inclusion bodies and the extent of solubility was compared with that of 8 M urea as well as 6 M Gdn-HCl. Hydrophobic interactions as well as ionic interactions were found to be the dominant forces responsible for the formation of r-hGH inclusion bodies during its high-level expression in E. coli. Complete solubilization of r-hGH inclusion bodies was observed in 100 mM Tris buffer at pH 12.5 containing 2 M urea. Solubilization of r-hGH inclusion bodies in the presence of low concentrations of urea helped in retaining the existing native-like secondary structures of r-hGH, thus improving the yield of bioactive protein during refolding. Solubilized r-hGH in Tris buffer containing 2 M urea was found to be less susceptible to aggregation during buffer exchange and thus was refolded by simple dilution. The r-hGH was purified by use of DEAE-Sepharose ion-exchange chromatography and the pure monomeric r-hGH was finally obtained by using size-exclusion chromatography. The overall yield of the purified monomeric r-hGH was approximately 50% of the initial inclusion body proteins and was found to be biologically active in promoting growth of rat Nb2 lymphoma cell lines.     

Optimization and efficient purification of recombinant Omp28 protein of Brucella melitensis using Triton X-100 and β-mercaptoethanol

The high level expression of recombinant proteins in Escherichia coli often leads to the formation of inclusion bodies that contain most of the expressed protein held together by non-covalent forces. The inclusion bodies are usually solubilized using strong denaturing agents like urea and guanidium hydrochloride. In this study recombinant Omp28 (rOmp28) protein of Brucella melitensis was expressed in two different vector systems and further efficient purification of the protein was done by modification in buffers to improve the yield and purity. Different concentrations of Triton X-100 and β-mercaptoethanol were optimized for the solubilization of inclusion bodies. The lysis buffer with 8M urea alone was not sufficient to solubilize the inclusion bodies. It was found that the use of 1% Triton X-100 and 20mM β-mercaptoethanol in lysis and wash buffers used at different purification steps under denaturing conditions increased the yield of purified rOmp28 protein. The final yield of purified protein obtained with modified purification protocol under denaturing conditions was 151 and 90mg/l of the culture or 11.8 and 9.37mg/g of wet weight of cells in pQE30UA and pET28a(+) vector respectively. Thus modified purification protocol yielded more than threefold increase of protein in pQE30UA as compared with purification by conventional methods.     

Inclusion body purification and protein refolding using microfiltration and size exclusion chromatography

The presence of inclusion body impurities can affect the refolding yield of recombinant proteins, thus there is a need to purify inclusion bodies prior to refolding. We have compared centrifugation and membrane filtration for the washing and recovery of inclusion bodies of recombinant hen egg white lysozyme (rHEWL). It was found that the most significant purification occurred during the removal of cell debris. Moderate improvements in purity were subsequently obtained by washing using EDTA, moderate urea solutions and Triton X-100. Centrifugation between each wash step gave a purer product with a higher rHEWL yield. With microfiltration, use of a 0.45 micron membrane gave higher solvent fluxes, purer inclusion bodies and greater protein yield as compared with a 0.1 micron membrane. Significant flux decline was observed for both membranes. Second, we studied the refolding of rHEWL. Refolding from an initial concentration of 1.5 mg ml-1, by 100-fold batch dilution gave a 43% recovery of specific activity. Purified inclusion bodies gave rise to higher refolding yields, and negligible activity was observed after refolding partially purified material. Refolding rHEWL with a size exclusion chromatography based process gave rise to a refolding yield of 35% that corresponded to a 20-fold dilution.     

Partition features and renaturation enhancement of chymosin in aqueous two-phase systems

Aqueous two-phase systems of polyethylene glycol (molecular mass 1450, 3350 and 6000)-phosphate and polyethylene-polypropylene oxide (molecular mass 8400)-maltodextrin systems were used in order to study the partition features of recombinant chymosin from inclusion bodies. These systems in the presence of 8M urea were used for the solubilization of inclusion bodies containing recombinant chymosin and for the oxidative renaturation of this protein. Recombinant chymosin showed to be partitioned in favour of the top phase in all studied systems with a partition coefficient between 4 and 6. The recovery of the chymosin biological activity was 32% in the polyethylene-polypropylene oxide, while in the polyethylene glycol-phosphate the recovery was 50-59%. The results indicate that the liquid-liquid extraction would be an adequate tool able to isolate and concentrate chymosin from inclusion bodies with a yield of biological activity higher than that obtained from the standard method (43%).     

提高成纤维细胞生长因子-21产率和纯度

成纤维细胞生长因子-21(FGF-21)作为近期发现的新型代谢调节因子,因其具有独立于胰岛素调节糖脂代谢、增加胰岛素敏感性等作用,有望成为治疗糖尿病的新型药物。包涵体形式表达外源蛋白表达量及纯度高,但是以pET载体表达时,FGF-21以包涵体形式表达,且复性率及产率低,蛋白活性降低[1]。针对这一瓶颈问题,用SUMO载体首次以包涵体形式表达带有SUMO标签的hFGF-21,通过优化培养条件,并应用中空纤维柱膜过滤技术对菌体进行富集,对包涵体进行洗涤、变性及复性,经过亲和层析、凝胶过滤层析的纯化方法,得到了成熟的hFGF-21,在保证蛋白活性的同时增加了蛋白的产量及纯度。通过检测HepG2细胞葡萄糖吸收及2型糖尿病db/db小鼠短期及长期血糖变化鉴定其降糖生物学活性。结果表明,以包涵体形式表达hFGF-21(ihFGF-21)的表达量是可溶形式表达的hFGF-21(shFGF-21)的3倍,最终ihFGF-21的收率为20 mg/L,而shFGF-21的收率仅为6 mg/L。ihFGF-21的纯度可达到95%以上,而shFGF-21仅能达到90%左右;在细胞水平和动物水平上两者的降糖生物学活性一致。在保证hFGF-21生物学活性的前提下,与传统包涵体途径提取目的蛋白的方法相比,应用中空纤维柱膜过滤技术使hFGF-21的生产周期缩短了约1/3左右。综上所述,此法为FGF-21中试及工业化生产提供了高效、经济的策略。     

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.     

Effect of operating variables on the yield of recombinant trypsinogen for a pulse-fed dilution-refolding reactor.

The inclusion body process route for manufacturing proteins offers distinct process advantages in terms of expression levels and the ease of initial inclusion body recovery. The efficiency of the refolding unit operation, however, does determine the overall economic feasibility of a process. Dilution refolding is the simplest and most extensively used refolding operation, although significant yield losses often occur due mainly to aggregation. Operating variables may have a significant effect on the degree of aggregation, but a systematic study has not been reported. This study investigates the effect of operating variables on the dilution refolding of solubilized r-trypsinogen inclusion bodies in a pulse-fed stirred reactor. Variables investigated were inclusion body washing, stirring speed, feed rate, concentration of solubilized r-trypsinogen, and concentration of urea during solubilization of the inclusion bodies. Additionally, the effect of baffles in the reactor was investigated. The yield of renatured r-trypsinogen varied between 12 +/- 0.2% and 21 +/- 1.0% depending on the specific combination of operating variables employed. It is clear that a suboptimal operating strategy can significantly reduce protein yield. In particular, we note that an increased intensity of mixing adversely affected yield in contrast to previous reports indicating that enhanced dispersion increases yield. We conclude that yield is determined not only by the efficiency of dispersion, but also by the local chemical environment of the protein as it folds, and the rate of change of this environment. This will be controlled by micromixing effects, and hence the intensity of agitation, in a complex manner requiring further characterization.     

Convenient and efficient in vitro folding of disulfide-containing globular protein from crude bacterial inclusion bodies

We investigated how the folding yield of disulfide-containing globular proteins having positive net charges from crude bacterial inclusion bodies was affected by additives in the folding buffer. In screening folding conditions for human ribonucleases and its derivative, we found that addition of salt (about 0.4 M) to a folding buffer increased the folding yield. This suggested that electrostatic interaction between polyanionic impurities such as nucleic acids and cationic unfolded protein led to the formation of aggregates under the low-salt conditions. Since inclusion bodies were found to contain nucleic acids regardless of the electrostatic nature of the expressed protein, the electrostatic interaction between phosphate moieties of nucleic acids and basic amino acid residues of a denatured protein may be large enough to cause aggregation, and therefore the addition of salt in a folding buffer may generally be useful for promotion of protein folding from crude inclusion bodies. We further systematically investigated additives such as glycerol, guanidium chloride, and urea that are known to act as chemical chaperons, and found that these additives, together with salt, synergistically improved folding yield. This study, suggesting that the addition of salt into the folding buffer is one of the crucial points to be considered, may pave the way for a systematic investigation of the folding conditions of disulfide-containing foreign proteins from crude bacterial inclusion bodies.     

口蹄疫病毒免疫活性串联片段FB的表达及免疫原性测定(英)

将口蹄疫病毒(FMDV)免疫串联片段FB克隆至原核表达载体pBAD/TOPO中,经鉴定后得到重组质粒pBAD-FB,将此重组质粒转化到受体菌TOP10中,用诱导剂阿拉伯醛糖分别以不同的浓度进行诱导,并在不同诱导时间进行采样,经处理后做SDS-聚丙烯酰胺凝胶电泳(SDS-PAGE)、蛋白质印迹分析.结果发现以终浓度为0.002%的阿拉伯醛糖进行诱导,4 h后表达可达到高峰,其大小约为26 ku,软件扫描结果显示,FB融合蛋白的表达量占细菌总蛋白的28.9%,能与抗FMDV抗体发生特异性反应,融合蛋白以包涵体和可溶形式存在.将融合蛋白的可溶性组分用50% Ni-NTA树脂过柱纯化并抽提融合蛋白的包涵体,经过洗涤后分别制成油乳剂疫苗,经皮下注射免疫豚鼠,用乳鼠中和试验测定豚鼠血清中和指数,并用口蹄疫病毒对豚鼠进行攻毒.结果表明,用此融合蛋白的纯化产物和包涵体免疫豚鼠能诱导产生高滴度的中和抗体,对病毒的攻击提供100%的免疫保护.     

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％。     

Production of nonclassical inclusion bodies from which correctly folded protein can be extracted

Human granulocyte-colony stimulating factor (hG-CSF), an important biopharmaceutical drug used in oncology, is currently produced mainly in Escherichia coli. Expression of human hG-CSF gene in E. coli is very low, and therefore a semisynthetic, codon-optimized hG-CSF gene was designed and subcloned into pET expression plasmids. This led to a yield of over 50% of the total cellular proteins. We designed a new approach to biosynthesis at low temperature, enabling the formation of "nonclassical" inclusion bodies from which correctly folded protein can be readily extracted by nondenaturing solvents, such as mild detergents or low concentrations of polar solvents such as DMSO and nondetergent sulfobetaines. FT-IR analysis confirmed different nature of inclusion bodies with respect to the growth temperature and indicated presence of high amounts of very likely correctly folded reduced hG-CSF in nonclassical inclusion bodies. The yield of correctly folded, functional hG-CSF obtained in this way exceeded 40% of the total hG-CSF produced in the cells and is almost completely extractable under nondenaturing conditions. The absence of the need to include a denaturation/renaturation step in the purification process allows the development of more efficient processes characterized by higher yields and lower costs and involving environment-friendly technologies. The technology presented works successfully at the 50-L scale, producing nonclassical inclusion bodies of the same quality. The approach developed for the production of hG-CSF could be extended to other proteins; thus, a broader potential for industrial exploitation is envisaged.     

重组刺桐胰蛋白酶抑制剂a在大肠杆菌中的表达和纯化

为了大量制备重组刺桐胰蛋白酶抑制剂a(rETIa) ,对构建的基因工程菌株E .coliBL2 1(DE3)pET2 2b mETIa进行了表达条件的优化 .用摇瓶培养 ,rETIa蛋白占菌体总蛋白 4 0 %以上 .经破碎菌体 洗涤包涵体 溶解包涵体 复性初步纯化后 ,再经二步柱层析纯化获得电泳纯的rETIa蛋白 .测定了rETIa对胰蛋白酶、胰凝乳蛋白酶、组织型纤溶酶原激活因子缺失突变体 (NTA)的抑制活性 .     

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.     

Improved Recovery of a Fusion Protein Containing the Antigenic Domain 1 of the Human Cytomegalovirus Glycoprotein B

Heterologous expression in Escherichia coli often leads to production of the expressed proteins as insoluble and inactive inclusion bodies. The general strategy for protein recovery includes isolation and washing of inclusion bodies, solubilization of aggregated protein and refolding of solubilized protein. The process of refolding, as well as the other steps involved in inclusion body recovery, must be optimized according to the characteristics of each protein. For the development of reliable and inexpensive serodiagnostic tests, the antigenic domain 1 (AD-1) of human cytomegalovirus glycoprotein B was expressed in E. coli and a process was developed to increase recovery of the fusion protein containing AD-1. A comparison of disruption methods and different conditions involved in recovery of this fusion protein from inclusion bodies is presented. The developed method gives a high yield of the fusion protein with a purity sufficient for use in diagnostic tests.     

A crosslinked inclusion body process for sialic acid synthesis

The propensity of a recombinant protein produced in bacteria to aggregate has been assumed to be unpredictable, and inclusion bodies have been thought of as wasted cell material. However, a target protein can be purposely driven to inclusion bodies, which demonstrate full cell tolerable activity. Sialic acid aldolase, N-terminally fused with the cellulose-binding module of Clostridium cellulovorans, was almost quantitatively physiologically aggregated into active inclusion bodies. These inclusion bodies were entrapped in alginate beads and crosslinked by glutaraldehyde. The immobilized biocatalyst generated by this crosslinked inclusion bodies (CLIB) technology was used in a repetitive batch protocol for sialic acid production that was monitored on-line by flow calorimetry. The required substrate, N-acetyl-D-mannosamine, was obtained by partially improved alkaline epimerization.     

Improving the soluble expression of aequorin in Escherichia coli using the chaperone-based approach by co-expression with artemin

Abstract

Escherichia coli is a common host that is widely used for producing recombinant proteins. However, it is a simple approach for production of heterologous proteins; the major drawbacks in using this organism include incorrect protein folding and formation of disordered aggregated proteins as inclusion bodies. Co-expression of target proteins with certain molecular chaperones is a rational approach for this problem. Aequorin is a calcium-activated photoprotein that is often prone to form insoluble inclusion bodies when overexpressed in E. coli cells resulting in low active yields. Therefore, in the present research, our main aim is to increase the soluble yield of aequorin as a model protein and minimize its inclusion body content in the bacterial cells. We have applied the chaperone-assisted protein folding strategy for enhancing the yield of properly folded protein with the assistance of artemin as an efficient molecular chaperone. The results here indicated that the content of the soluble form of aequorin was increased when it was co-expressed with artemin. Moreover, in the co-expressing cells, the bioluminescence activity was higher than the control sample. We presume that this method might be a potential tool to promote the solubility of other aggregation-prone proteins in bacterial cells.     

Immunogenicity of in vitro folded outer membrane protein PorA of Neisseria meningitidis

In vitro folded and the denatured form of PorA P1.6 from Neisseria meningitidis strain M990 were used for immunization studies in mice. Previously, the antigen was isolated from cytoplasmic inclusion bodies, folded and purified. Its immunogenicity without adjuvant appeared to be low. The addition of the adjuvant QuilA, but not of galE lipooligosaccharide, considerably enhanced the immunogenicity. Moreover, when immunized with folded PorA P1.6 plus QuilA, a clear switch towards the IgG2a subclass of antibodies and concomitantly, the appearance of serum bactericidal activity, which is believed to be important for protective immunity, was observed. Hence, a tool for preparing vaccines against serogroup B meningococci devoid of endotoxin is available.     

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%.