Expression of recombinant Streptolysin O and specific antibody production

Streptolysin O (SLO), an oxygen-labile cytolysin, is the cholesterol-binding exotoxin of hemolytic streptococci. Besides microbiological and pathological interests, this cytolysin has been used as a tool for permeabilization of biomembranes. SLO serves as a diagnostic reagent for determination of anti-SLO antibody titer in streptococcal infection. Availability of highly purified SLO, however, has been limited by low yield in streptococcal culture and purification process. Present subcloning of mature-type full-length SLO gene into an expression vector having strictly controllable araBAD promoter enabled efficient production of the cytolysin. Further, anti-SLO antibody with high specificity was obtained by immunizing with purified SLO protein.     

Specificity of streptolysin O in cytolysin-mediated translocation

Cytolysin-mediated translocation (CMT) is a recently described process in the Gram-positive pathogen Streptococcus pyogenes that translocates an effector protein of streptococcal origin into the cytoplasm of a host cell. At least two proteins participate in CMT, the pore-forming molecule streptolysin O (SLO) and an effector protein with the characteristics of a signal transduction protein, the Streptococcus pyogenes NAD-glycohydrolase (SPN). In order to begin to elucidate the molecular details of the translocation process, we examined whether perfringolysin O (PFO), a pore-forming protein related to SLO, could substitute for SLO in the translocation of SPN. When expressed by S. pyogenes, PFO, like SLO, had the ability to form functional pores in keratinocyte membranes. However, unlike SLO, PFO was not competent for translocation of SPN across the host cell membrane. Thus, pore formation by itself was not sufficient to promote CMT, suggesting that an additional feature of SLO was required. This conclusion was supported by the construction of a series of mutations in SLO that uncoupled pore formation and competence for CMT. These mutations defined a domain in SLO that was dispensable for pore formation, but was essential for CMT. However, introduction of this domain into PFO did not render PFO competent for CMT, implying that an additional domain of SLO is also critical for translocation. Taken together, these data indicate that SLO plays an active role in the translocation process that extends beyond that of a passive pore.     

Enhancement of streptolysin O activity and intrinsic cytotoxic effects of the group A streptococcal toxin, NAD-glycohydrolase

Streptolysin O (SLO) is a cholesterol-dependent cytolysin produced by the important human pathogen, group A Streptococcus (Streptococcus pyogenes or GAS). In addition to its cytolytic activity, SLO mediates the translocation of GAS NAD-glycohydrolase (NADase) into human epithelial cells in vitro. Production of both NADase and SLO is associated with augmented host cell injury beyond that produced by SLO alone, but the mechanism of enhanced cytotoxicity is not known. We have now shown that expression of NADase together with SLO dramatically enhanced the lytic activity of GAS culture supernatants for erythrocytes but had no effect on SLO-mediated poration of synthetic cholesterol-rich liposomes. This result revealed a previously unknown contribution of NADase to the cytolytic activity associated with GAS production of SLO. Purified recombinant SLO bound NADase in vitro, supporting a specific, physical interaction of the two proteins. Exposure of human keratinocytes to wild-type GAS, but not to a NADase-deficient mutant strain, resulted in profound depletion of cellular NAD+ and ATP. Furthermore, expression of recombinant GAS NADase in yeast, in the absence of SLO, induced growth arrest, depletion of NAD+ and ATP, and cell death. These findings have provided evidence that the augmentation of SLO-mediated cytotoxicity by NADase is a consequence of depletion of host cell energy stores through the enzymatic action of NADase. Together, the results have provided mechanistic insight into the cytotoxic effects of a unique bipartite bacterial toxin.     

表达重组人骨形态发生蛋白-7工程菌的发酵及表达产物的纯化

目的:研究表达重组人骨形态发生蛋白-7工程菌的发酵和表达产物的纯化工艺。方法:利用16L发酵罐发酵培养工程菌,设定了溶氧、搅拌速度、诱导时机、补料和培养基pH值等发酵条件;通过包涵体洗涤、离子交换层析法纯化目的蛋白。结果:工程菌目的蛋白质表达量占菌体总蛋白质的30%以上,纯化后目的蛋白的纯度可达98%。结论:建立了大肠杆菌高效表达人骨形态发生蛋白-7的发酵及纯化工艺。     

Construction of intein-mediated hGMCSF expression vector and its purification in Pichia pastoris

As a novel attempt for the intracellular recombinant protein over expression and easy purification from Pichia pastoris, the therapeutic cytokine human granulocyte macrophage colony stimulating factor (hGMCSF) gene was fused to an intein-chitin-binding domain (gene from pTYB11 vector) fusion tag by overlap extension PCR and inserted into pPICZB vector, allowing for the purification of a native recombinant protein without the need for enzymatic cleavage. The fusion protein under the AOX1 promoter was integrated into the P. pastoris genome (SMD 1168) and the recombinant Pichia clones were screened for multicopy integrants. Expression of hGMCSF was done using glycerol and methanol based synthetic medium by three stage cultivation in a bioreactor. Purification of the expressed hGMCSF fusion protein was done after cell disruption and binding of the solubilized fusion protein to chitin affinity column, followed by DTT induced on column cleavage of hGMCSF from the intein tag. In this study, final biomass of 89 g dry cell weight/l and purified hGMCSF of 120 mg/l having a specific activity of 0.657 x 10(7) IU/mg was obtained. This strategy has an edge over the other--His or--GST based fusion protein purification where non-specific protein binding, expensive enzymatic cleavage and further purification of the enzyme is required. It distinguishes itself from all other purification systems by its ability to purify, in a single chromatographic step.     

Ultrastructural analysis of the membrane insertion of domain 3 of streptolysin O

Streptolysin O (SLO) is a membrane-damaging toxic protein produced by group A streptococci. We performed an ultrastructural analysis of pore formation and the mechanism of hemolysis by SLO, using a mutant form of SLO [SLO(C/A)-SS] and native SLO. SLO(C/A)-SS was unable to penetrate the erythrocyte membrane as a consequence of immobilization that was due to a disulfide bond between domains. The SLO(C/A)-SS molecules that bound to membranes formed numerous single-layered ring-shaped structures that did not result in pores on the membranes. These structures were similar to the structures formed by native SLO at 0 degrees C. After treatment with dithiothreitol, SLO(C/A)-SS that had bound to membranes formed double-layered rings with pores on the membranes, as does native SLO at room temperature. Our morphological evidence demonstrates that an increase in temperature is necessary for the occurrence of conformational changes and for the formation of double-layered rings after the insertion of domain 3 into the host cell membrane. On the basis of a model of the oligomeric structure of SLO, we propose some new details of the mechanism of hemolysis by SLO.     

Chemokine production by rat macrophages stimulated with streptolysin O from Streptococcus pyogenes

The contribution of streptolysin O (SLO) from Streptococcus pyogenes to neutrophil infiltration in inflammatory lesions was determined by production of cytokine-induced neutrophil chemoattractant (CINC)-1, -2 and -3, and macrophage inflammatory protein (MIP)-1alpha by rat macrophages stimulated with SLO in culture. Active SLO induced the production of CINCs and MIP-1alpha in dose- and time-dependent manners. These inductions were ascertained by chemokine mRNA expression in macrophages. Streptolysin S was without effect. The SLO-cholesterol complex induced the chemokine production in proportion to the residual hemolytic activity of the complex. In addition, the effects of SLO on the chemokine production were confirmed by the injection of active SLO into the preformed air pouch on the back of rats. The infiltration of neutrophils into the pouch fluid (exudate) increased steadily with a lag phase of about 2 hr. The major chemokine found in exudates was MIP-1alpha but not CINCs. In this study, it became clear that active SLO, but not the inactive one, contributed to the production of MIP-1alpha and CINCs in the conditioned medium and in exudates.     

Expression and purification of recombinant nattokinase in <Emphasis Type="Italic">Spodoptera frugiperda</Emphasis> cells

A recombinant baculovirus, rv-egfp-NK, containing a reporter gene encoding the enhanced green fluorescent protein (EGFP), was used to express nattokinase (NK), a fibrinolytic enzyme, in Spodoptera frugiperda (SF-9) cells. The recombinant protein also included a histidine tag for purification using Ni(2+) resins. The recombinant NK, approximately 30 kDa, retained fibrinolytic activity (60 U/ml). The integration of the EGFP expression cassette in the Bac-to-Bac system is thus an effective method for the expression and purification of recombinant NK protein in Spodoptera frugiperda insect cells.     

Purification and partial characterization of recombinant Cu, Zn containing superoxide dismutase of Cordyceps militaris in E.coli

The cDNA of Cu, Zn containing superoxide dismutase from the Cordyceps militaris SH (cm-SOD) was overexpressed in Escherichia coli BL 21 (DE3) using the pET-21a expression vector. The recombinant cell overexpressed the protein corresponding to 35+/-3% of total bacterial protein in cytosol. The purification was performed through three steps: DEAE-FF, CM-52, and G-100. After this purification procedure, a specific activity of 27272.7 U/mg of protein was reached, corresponding to 6.1-fold purification with a yield of 85.0%. The purity was homogeneous by SDS-PAGE analysis and 94.2+/-1.0% by CZE analysis. A subunit molecular mass of the recombinant enzyme was 15704 Da with a Cu and Zn element. In addition, the dimeric and polymeric structures were observed on MALDI-TOF-MS. Isoelectric point value of 7.0 was obtained for the recombinant enzyme that was sensitive to H2O2 and KCN. The recombinant enzyme remained 80+/-2% residual activity at pH 7.8, at 50 degrees C for 4h incubation. The properties: N-terminal amino acid sequence (the first 12 amino acid residues), pI, subunit molecular mass, thermo-stability of the purified recombinant SOD are similar to that of the native Cu, Zn-SOD from C. militaris (N-cm-SOD).     

Protein production from recombinant protein bodies

In this study, we describe a process for protein expression and purification from plants and insect cells based on the accumulation of recombinant proteins in protein bodies. This technology is using Zera^®, which sequence has the capacity to trigger in vivo the formation of dense, non-secretory storage protein body-like organelles derived from the endoplasmic reticulum (ER). With this method, recombinant human growth hormone (hGH) was expressed and purified from protein bodies accumulated in plants (Nicotiana benthamiana) and in insect cells (Spodoptera frugiperda). We found that recombinant Zera-hGH are stored in large quantity inside those proteins bodies and can be easily recovered during a one-step process from plant and insect cell biomass. After solubilization of recombinant protein bodies and cleavage of Zera tag from the fusion protein, active hGH was finally purified by a single chromatography step. These results indicate that recombinant proteins derived from Zera-fusion could provide both an efficient protein production system and eased purification downstream process.     

Plasmid vectors for proteomic analyses in Giardia: purification of virulence factors and analysis of the proteasome

In recent years, proteomics has come of age with the development of efficient tools for purification, identification, and characterization of gene products predicted by genome projects. The intestinal protozoan Giardia intestinalis can be transfected, but there is only a limited set of vectors available, and most of them are not user friendly. This work delineates the construction of a suite of cassette-based expression vectors for use in Giardia. Expression is provided by the strong constitutive ornithine carbamoyltransferase (OCT) promoter, and tagging is possible in both N- and C-terminal configurations. Taken together, the vectors are capable of providing protein localization and production of recombinant proteins, followed by efficient purification by a novel affinity tag combination, streptavidin binding peptide-glutathione S-transferase (SBP-GST). The option of removing the tags from purified proteins was provided by the inclusion of a PreScission protease site. The efficiency and feasibility of producing and purifying endogenous recombinant Giardia proteins with the developed vectors was demonstrated by the purification of active recombinant arginine deiminase (ADI) and OCT from stably transfected trophozoites. Moreover, we describe the tagging, purification by StrepTactin affinity chromatography, and compositional analysis by mass spectrometry of the G. intestinalis 26S proteasome by employing the Strep II-FLAG-tandem affinity purification (SF-TAP) tag. This is the first report of efficient production and purification of recombinant proteins in and from Giardia, which will allow the study of specific parasite proteins and protein complexes.     

Recombinant aprotinin produced in transgenic corn seed: extraction and purification studies

Expression in transgenic plants is potentially one of the most economical systems for large-scale production of valuable peptide and protein products. However, the downstream processing of recombinant proteins produced in plants has not been extensively studied. In this work, we studied the extraction and purification of recombinant aprotinin, a protease inhibitor used as a therapeutic compound, produced in transgenic corn seed. Conditions for extraction from transgenic corn meal that maximize aprotinin concentration and its fraction of the total soluble protein in the extract were found: pH 3.0 and 200 mM NaCl. Aprotinin, together with a native corn trypsin inhibitor (CTI), was captured using a tryspin-agarose column. These two inhibitors were separated using an agarose-IDA-Cu2+ column that proved to efficiently absorb the CTI while the recombinant aprotinin was collected in the flowthrough with purity of at least 79%. The high purity of the recombinant aprotinin was verified by SDS-PAGE and N-terminal sequencing. The overall recombinant aprotinin recovery yield and purification factor were 49% and 280, respectively. Because CTI was also purified, the recovery and purification process studied has the advantage of possible CTI co-production. Finally, the work presented here introduces additional information on the recovery and purification of recombinant proteins produced in plants and corroborates with past research on the potential use of plants as biorreactors.     

Purification of recombinant protein by cold‐coacervation of fusion constructs incorporating resilin‐inspired polypeptides

Polypeptides containing between 4 and 32 repeats of a resilin‐inspired sequence AQTPSSYGAP, derived from the mosquito Anopheles gambiae, have been used as tags on recombinant fusion proteins. These repeating polypeptides were inspired by the repeating structures that are found in resilins and sequence‐related proteins from various insects. Unexpectedly, an aqueous solution of a recombinant resilin protein displays an upper critical solution temperature (cold‐coacervation) when held on ice, leading to a separation into a protein rich phase, typically exceeding 200 mg/mL, and a protein‐poor phase. We show that purification of recombinant proteins by cold‐coacervation can be performed when engineered as a fusion partner to a resilin‐inspired repeat sequence. In this study, we demonstrate the process by the recombinant expression and purification of enhanced Green fluorescent protein (EGFP) in E. coli. This facile purification system can produce high purity, concentrated protein solutions without the need for affinity chromatography or other time‐consuming or expensive purification steps, and that it can be used with other bulk purification steps such as low concentration ammonium sulfate precipitation. Protein purification by cold‐coacervation also minimizes the exposure of the target protein to enhanced proteolysis at higher temperature. Biotechnol. Bioeng. 2012; 109: 2947–2954. © 2012 Wiley Periodicals, Inc.     

Intein-mediated protein purification of fusion proteins expressed under high-cell density conditions in E. coli

The intein-mediated purification system has the potential to significantly reduce the recovery costs of industrial recombinant proteins. The ability of inteins to catalyze a controllable peptide bond cleavage reaction can be used to separate a recombinant protein from its affinity tag during affinity purification. Inteins have been combined with a chitin-binding domain to serve as a self-cleaving affinity tag, facilitating highly selective capture of the fusion protein on an inexpensive substrate--chitin (IMPACT) system, New England Biolabs, Beverly, MA). This purification system has been used successfully at a lab scale in low cell density cultures, but has not been examined comprehensively under high-cell density conditions in defined medium. In this study, the intein-mediated purification of three commercially relevant proteins expressed under high-cell density conditions in E. coli was studied. Additionally, losses during the purification process were quantified. The data indicate that the intein fusion proteins expressed under high cell density fermentations were stable in vivo after induction for a significant duration, and the intein fusion proteins could undergo thiol or pH and temperature initiated cleavage reaction in vitro. Thus, the intein-mediated protein purification system potentially could be employed for the production of recombinant proteins at the industrial-scale.     

Phosphorylation of Glutathione-S-transferase by Protein Kinase C-α Implications for Affinity-Tag Purification

Expression and purification of proteins as fusions with glutathione S-transferase (GST) is a standard and widely employed system. In more than 2,500 published studies, GST has been used to facilitate the purification of recombinant proteins, assess protein-protein interactions, and establish protein function. In this report, we provide evidence that GST can be phosphorylated in vitro by protein kinase C-alpha (PKC-alpha) at Ser-93. Therefore, since GST itself may be a target for a number of catalytic enzymes, failure to remove the GST tag from the recombinant protein may lead to inaccurate conclusions.     

Expression and purification of mammalian calreticulin in Pichia pastoris

Calreticulin is a 46-kDa Ca(2+)-binding chaperone of the endoplasmic reticulum membranes. The protein binds Ca(2+) with high capacity, affects intracellular Ca(2+) homeostasis, and functions as a lectin-like chaperone. In this study, we describe expression and purification procedures for the isolation of recombinant rabbit calreticulin. The calreticulin was expressed in Pichia pastoris and purified to homogeneity by DEAE-Sepharose and Resource Q FPLC chromatography. The protein was not retained in the endoplasmic reticulum of Pichia pastoris but instead it was secreted into the external media. The purification procedures reported here for recombinant calreticulin yield homogeneous preparations of the protein by SDS-PAGE and mass spectroscopy analysis. Purified calreticulin was identified by its NH(2)-terminal amino acid sequences, by its Ca(2+) binding, and by its reactivity with anti-calreticulin antibodies. The protein contained one disulfide bond between (88)Cys and (120)Cys. CD spectral analysis and Ca(2+)-binding properties of the recombinant protein indicated that it was correctly folded.     

Affinity purification of streptavidin using tobacco mosaic virus particles as purification tags

A new protein affinity purification system has been developed. Recombinant tobacco mosaic virus (TMV) was used as an affinity matrix for isolation and purification of the given protein of interest. In model experiments, streptavidin-specific heptapeptide sequence TLIAHPQ was inserted into TMV coat protein near the C end. This oligopeptide did not interfere significantly with viral replication, assembly, and movement. Recombinant TMV functioned as an epitope tag recognizing streptavidin in plant protein extracts. Plant protein extracts containing streptavidin were incubated with recombinant TMV virions. Affinity complexes of viral particles with the protein of interest were collected by centrifugation. Recombinant TMV-streptavidin complex was dissociated with 0.2M acetic acid, pH 4.6, and was passed through membrane filter Nanosep 300K by centrifugation. The filtrate contained pure streptavidin. Recombinant TMV was left on the filter. TMV particles collected from the filter could be used for at least two more purification cycles. The streptavidin-specific recombinant TMV system was applied successfully for purification of streptavidin from Streptomyces avidinii. The authors believe that the TMV-based affinity system can also be used for the purification of other proteins.     

Noncytotoxic inhibition of cytomegalovirus replication through NK cell protease granzyme M-mediated cleavage of viral phosphoprotein 71

Granzyme M (GrM) is highly expressed in cytotoxic granules of NK cells, which provide the first line of defense against viral pathogens. GrM knockout mice show increased susceptibility toward murine CMV infection. Although GrM is a potent inducer of cell death, the mechanism by which GrM eliminates viruses remains elusive. In this paper, we show that purified human GrM in combination with the perforin-analog streptolysin O (SLO) strongly inhibited human CMV (HCMV) replication in fibroblasts in the absence of host cell death. In a proteomic approach, GrM was highly specific toward the HCMV proteome and most efficiently cleaved phosphoprotein 71 (pp71), an HCMV tegument protein that is critical for viral replication. Cleavage of pp71 occurred when viral lysates were incubated with purified GrM, when intact cells expressing recombinant pp71 were challenged with living cytotoxic effector cells, and when HCMV-infected fibroblasts were incubated with SLO and purified GrM. GrM directly cleaved pp71 after Leu(439), which coincided with aberrant cellular localization of both pp71 cleavage fragments as determined by confocal immunofluorescence. In a luciferase reporter assay, cleavage of pp71 after Leu(439) by GrM completely abolished the ability of pp71 to transactivate the HCMV major immediate-early promoter, which is indispensable for effective HCMV replication. Finally, GrM decreased immediate-early 1 protein expression in HCMV-infected fibroblasts. These results indicate that the NK cell protease GrM mediates cell death-independent antiviral activity by direct cleavage of a viral substrate.     

Secretion and purification of recombinant beta1-4 galactosyltransferase from insect cells using pFmel-protA, a novel transposition-based baculovirus transfer vector

The palette of transfer vectors available for generation of recombinant baculoviruses based on transposition-mediated recombination has been enlarged by constructing the pFmel-protA vector. The pFmel-protA plasmid includes the honeybee melittin secretion signal and a Staphylococcus aureus protein A fusion protein tag, which allows the secretion and purification of recombinant proteins. Using this system, the human beta1-4 galactosyltransferase-I protein was expressed in Sf9 insect cells at a level ranging from 22 to 28 U (4.8 to 6.0 mg)/L. The protein A tag enabled a simple monitoring of recombinant protein expression by enzyme-linked immunosorbent assay and Western blotting. Single step purification was achieved by immunoglobulin G affinity chromatography achieving a recovery yield of 28% and a specific activity of 1.9 U per mg of recombinant protein.     

Study of protein splicing and intein-mediated peptide bond cleavage under high-cell-density conditions

Protein splicing elements (inteins), capable of catalyzing controllable peptide bond cleavage reactions, have been used to separate recombinant proteins from affinity tags during affinity purification. Since the inteins eliminate the use of a protease in the recovery process, the intein-mediated purification system has the potential to significantly reduce recovery costs for the industrial production of recombinant proteins. Thus far, the intein system has only been examined and utilized for expression and purification of recombinant proteins at the laboratory scale for cells cultivated at low cell densities. In this study, protein splicing and in vitro cleavage of intein fusion proteins expressed in high-cell-density fed-batch fermentations of recombinant Escherichia coli were examined. Three model intein fusion constructs were used to examine the stability and splicing/cleavage activities of the fusion proteins produced under high-cell-density conditions. The data indicated that the intein fusion protein containing the wild-type intein catalyzed efficient in vivo protein splicing during high-cell-density cultivation. Also, the intein fusion proteins containing modified inteins catalyzed efficient thiol-induced in vitro cleavage reactions. The results of this study demonstrated the potential feasibility of using the intein-mediated protein purification system for industrial-scale production of recombinant proteins.