Penicillin-binding protein 2a of Streptococcus pneumoniae: expression in Escherichia coli and purification and refolding of inclusion bodies into a soluble and enzymatically active enzyme.

Penicillin-binding proteins (PBPs), targets of beta-lactam antibiotics, are membrane-bound enzymes essential for the biosynthesis of the bacterial cell wall. PBPs possess transpeptidase and transglycosylase activities responsible for the final steps of the bacterial cell wall cross-linking and polymerization, respectively. To facilitate our structural studies of PBPs, we constructed a 5'-truncated version (lacking bp from 1 to 231 encoding the N-terminal part of the protein including the transmembrane domain) of the pbp2a gene of Streptococcus pneumoniae and expressed the truncated gene product as a GST fusion protein in Escherichia coli. This GST fusion form of PBP2a, designated GST-PBP2a*, was expressed almost exclusively as inclusion bodies. Using a combination of high- and low-speed centrifugation, large amounts of purified inclusion bodies were obtained. These purified inclusion bodies were refolded into a soluble and enzymatically active enzyme using a single-step refolding method consisting of solubilization of the inclusion bodies with urea and direct dialysis of the solubilized preparations. Using these purification and refolding methods, approximately 37 mg of soluble GST-PBP2a* protein was obtained from 1 liter of culture. The identity of this refolded PBP2a* protein was confirmed by N-terminal sequencing. The refolded PBP2a*, with or without the GST-tag, was found to bind to BOCILLIN FL, a beta-lactam, and to hydrolyze S2d, an analog of the bacterial cell wall stem peptides. The S2d hydrolysis activity of PBP2a* was inhibited by penicillin G. In conclusion, using this expression system, and the purification and refolding methods, large amounts of the soluble GST-PBP2a* protein were obtained and shown to be enzymatically active.     

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%.     

Refolding and purification of yeast carboxypeptidase Y expressed as inclusion bodies in Escherichia coli

The genes encoding carboxypeptidase Y (CPY) and CPY propeptide (CPYPR) from Saccharomyces cerevisiae were cloned and expressed in Escherichia coli. Six consecutive histidine residues were fused to the C-terminus of the CPYPR for facilitated purification. High-level expression of CPY and CPYPR-His(6) was achieved but most of the expressed proteins were present in the form of inclusion bodies in the bacterial cytoplasm. The CPY and CPYPR-His(6) produced as inclusion bodies were separated from the cells and solubilized in 6 and 3 M guanidinium chloride, respectively. The denatured CPYPR-His(6) was refolded by dilution 1:30 into the renaturation buffer (50 mM Tris-HCl containing 0.5 M NaCl and 3 mM EDTA, pH 8.0), and the refolded CPYPR-His(6) was further purified to 90% purity by single-step immobilized metal ion affinity chromatography. The denatured CPY was refolded by dilution 1:60 into the renaturation buffer containing CPYPR-His(6) at various concentrations. Increasing the molar ratio of CPYPR-His(6) to CPY resulted in an increase in the CPY refolding yield, indicating that the CPYPR-His(6) plays a chaperone-like role in in vitro folding of CPY. The refolded CPY was purified to 92% purity by single-step p-aminobenzylsuccinic acid affinity chromatography. When refolding was carried out in the presence of 10 molar eq CPYPR-His(6), the specific activity, N-(2-furanacryloyl)-l-phenylalanyl-l-phenylalanine hydrolysis activity per milligram of protein, of purified recombinant CPY was found to be about 63% of that of native S. cerevisiae CPY.     

Cloning and purification of functionally active Fas ligand interfering protein (FIP) expressed in Escherichia coli

This report presents purification and characterization of the extracellular domain of rat Fas protein, called FIP (FasL interfering protein), expressed as inclusion bodies in Escherichia coli. FIP was extracted from the inclusion bodies, solubilized with 8 M urea, purified by a single-step immobilized metal ion (Ni(2+)) affinity chromatography and refolded. SDS/PAGE and mass spectrometry analysis of the purified protein verified its purity. Fluorescence spectrum analysis showed that the refolding procedure caused structural changes which presumably might have led to oligomerization. The purified FIP has biological activities: it binds specifically soluble Fas ligand and protects human Jurkat lymphocytes against FasL-dependent apoptosis. This efficient procedure of FIP expression in E. coli and renaturation may be useful for production of therapeutically important proteins.     

Purification of the Caenorhabditis elegans Transposase Tc1A Refolded during Gel Filtration Chromatography

Full-length recombinant transposase Tc1A from Caenorhabditis elegans (343 amino acids) expressed in Escherichia coli BL21 in inclusion bodies has been purified in a high yield in a soluble form. The procedure includes denaturation of the inclusion bodies followed by refolding of the Tc1A protein by gel filtration. This last step is absolutely crucial to give a high yield of soluble and active protein since it allows the physical separation of the aggregates from intermediates that give rise to correctly refolded protein. This step is very sensitive to the concentration of protein. Good yields of refolded protein are obtained by refolding 2 to 12 mg of denatured protein. The other purification steps involve the initial use of gel filtration under denaturing conditions and a final step of ion-exchange chromatography. Biological activity of the purified protein was confirmed in an in vitro transposon excision assay and its DNA-binding capacity by UV crosslinking. This new Tc1A purification procedure gives a yield of 12–16 mg/liter E. coli culture, in a form suitable for crystallization studies.     

Purification of the Caenorhabditis elegans transposase Tc1A refolded during gel filtration chromatography

Full-length recombinant transposase Tc1A from Caenorhabditis elegans (343 amino acids) expressed in Escherichia coli BL21 in inclusion bodies has been purified in a high yield in a soluble form. The procedure includes denaturation of the inclusion bodies followed by refolding of the Tc1A protein by gel filtration. This last step is absolutely crucial to give a high yield of soluble and active protein since it allows the physical separation of the aggregates from intermediates that give rise to correctly refolded protein. This step is very sensitive to the concentration of protein. Good yields of refolded protein are obtained by refolding 2 to 12 mg of denatured protein. The other purification steps involve the initial use of gel filtration under denaturing conditions and a final step of ion-exchange chromatography. Biological activity of the purified protein was confirmed in an in vitro transposon excision assay and its DNA-binding capacity by UV crosslinking. This new Tc1A purification procedure gives a yield of 12-16 mg/liter E. coli culture, in a form suitable for crystallization studies.     

Purification and characterization of recombinant sTRAIL expressed in Escherichia coli

As a potential anti-tumor protein, tumor necrosis factor-related apoptosis-inducing ligand(TRAIL) has drawn considerable attention. This report presented the purification and characterization ofsoluble TRAIL, expressed as inclusion bodies in E. coli. sTRAIL inclusion bodies were solubilized andrefolded at a high concentration up to 0.9 g/L by a simple dilution method. Refolded protein was purifiedto electrophoretic homogeneity by a single-step immobilized metal affinity chromatography. The purifiedsTRAIL had a strong cytotoxic activity against human pancreatic tumor cell line 1990, with EDs0 about 1.5mg/L. Circular dichroism and fluorescence spectrum analysis showed that the refolded sTRAIL had astructure similar to that of native protein with 13-sheet secondary structure. This efficient procedure ofsTRAIL renaturation may be useful for the mass production of this therapeutically important protein.     

尖吻蝮蛇毒酸性磷脂酶A_2I的表达及其生化特征

将尖吻蝮蛇毒酸性磷脂酶 Ａ２ Ｉ（ Ａ．ａ Ａ Ｐ Ｌ Ａ２ Ｉ） 的基因克隆至表达载体ｐ Ｂ Ｌ Ｍ Ｖ Ｌ２ , 在大肠杆菌 Ｒ Ｒ１ 中成功表达。表达产物 Ａ．ａ Ａ Ｐ Ｌ Ａ２ Ｉ约占细菌蛋白质总量的３０ ％ , 以包含体的形式存在。纯化包含体后, 将产物变性、复性, 然后用 Ｆ Ｐ Ｌ Ｃ Ｓｕｐｅｒｏｓｅ Ｔ Ｍ１２ 纯化, 产物经过 Ｓ Ｄ Ｓ Ｐ Ａ Ｇ Ｅ 检测只有单一条带。对表达的 Ａ．ａ Ａ Ｐ Ｌ Ａ２ Ｉ进行了酶活性、抑制血小板聚集活性和溶血活性的测定。结果显示, 表达的 Ａ．ａ Ａ Ｐ Ｌ Ａ２ Ｉ的酶活性同变性后复性江浙蝮蛇酸性磷脂酶 Ａ２（ Ａ Ｐ Ｌ Ａ２） 的酶活性相近, 既具有抑制血小板聚集活性也具有溶血活性。最后对磷脂酶 Ａ２（ Ｐ Ｌ Ａ２） 的结构与这些活性的关系进行了讨论     

Efficient production of a folded and functional, highly disulfide-bonded beta-helix antifreeze protein in bacteria

The Tenebrio molitor thermal hysteresis protein has a cysteine content of 19%. This 84-residue protein folds as a compact beta-helix, with eight disulfide bonds buried in its core. Exposed on one face of the protein is an array of threonine residues, which constitutes the ice-binding face. Previous protocols for expression of this protein in recombinant expression systems resulted in inclusion bodies or soluble but largely inactive material. A long and laborious refolding procedure was performed to increase the fraction of active protein and isolate it from inactive fractions. We present a new protocol for production of fully folded and active T. molitor thermal hysteresis protein in bacteria, without the need for in vitro refolding. The protein coding sequence was fused to those of various carrier proteins and expressed at low temperature in a bacterial strain specially suited for production of disulfide-bonded proteins. The product, after a simple and robust purification procedure, was analyzed spectroscopically and functionally and was found to compare favorably to previously published data on refolded protein and protein obtained from its native source.     

尖吻蝮蛇毒碱性磷脂酶A2的表达及其生化特征

将尖吻蝮蛇毒碱性磷脂酶A2 (A .aBPLA2 )基因克隆至温敏表达载体 pBLMVL2 ,在大肠杆菌RR1中成功诱导表达 .表达产物A .aBPLA2 约占细菌蛋白质总量的 2 0 % ,并以包涵体的形式存在 .纯化包涵体后 ,将产物变性、复性 ,然后用FPLCSuperoseTM12纯化 ,产物经过SDS 聚丙烯酰胺凝胶电泳检测只有单一条带 .对纯化后的表达A .aBPLA2 进行了酶活性、抑制血小板聚集活性和溶血活性的测定 .结果显示 ,表达A .aBPLA2的酶活性与变性后复性江浙蝮蛇酸性磷脂酶A2 酶活性相近 ,具有类似变性后复性江浙蝮蛇碱性磷脂酶A2 的溶血活性 ,没有抑制血小板聚集活性 .最后对磷脂酶A2 的结构与这些活性的关系进行了讨论     

Overproduction of single-chain antibodies against human IFN-alpha2B in Escherichia coli and their isolation in biologically active form

The gene encoding mouse single chain antibody (ScFv) against human interferon alpha2b (IFN-alpha2b) was cloned into the plasmid vector under the control of promoter from phage T7 and the recombinant protein was expressed in Escherichia coli as inclusion bodies. After the isolation of inclusion bodies the desired protein containing affinity tail "6His tag" was solubilized and purified under denaturing conditions by immobilized-metal affinity chromatography. The soluble and purified ScFv was obtained by "on column" refolding and the recovery of biological activity were demonstrated. The higher levels of ScFv production for intracellular expression system in comparison with ScFv obtained by secretion were shown. The advantages of described refolding method are simplicity and high efficacy, moreover, refolding using a chromatographic process represents the manufacturable approach because it is easily automated using commercially available materials and preparative chromatography systems and also can be combined with simultaneous purification.     

Refolding of the full-length non-structural protein 3 of hepatitis C virus

An easy and reproducible procedure for purification and refolding of the full-length non-structural protein 3 (NS3) from hepatitis C virus has been developed. Refolding was achieved by simply diluting the protein into a suitable buffer. Low protein concentration, high pH, highly reducing conditions, the presence of detergent, and low viscosity were important parameters for high refolding efficiency. Refolding was insignificantly affected by the presence of Zn(2+) in the refolding buffer, while the addition of NS4A cofactor inhibited refolding. A comparison of the kinetic parameters showed that the refolded enzyme is not as catalytically competent as the native enzyme. Nevertheless, the activity of the refolded NS3 protease was dependent on the specific NS4A-peptide cofactor and was inhibited by the specific substrate-based NS3 protease inhibitor, which indicates that the refolded NS3 can be appropriate for inhibitor screening. The yield of pure protein from the insoluble fraction of cell lysate was 6 mg/L of bacterial culture, which is 18 times higher than obtained from the soluble fraction. Improvement of the refolding conditions has resulted in a 50-fold higher activity of the protease as compared to refolding in buffer with neutral pH and no additives.     

Refolding and purification of Zymomonas mobilis levansucrase produced as inclusion bodies in fed-batch culture of recombinant Escherichia coli

Zymomonas mobilis levansucrase was overproduced by the fed-batch culture of recombinant Escherichia coli harboring a novel expression system that is constitutively expressed by the promoter from the Rahnella aquatilis levansucrase gene. Most of the levansucrase was produced as inclusion bodies in the bacterial cytoplasm, accounting for approximately 20% of the total cellular protein. Refolding after complete denaturation by high concentrations of urea or guanidine hydrochloride was not successful, resulting in large amounts of insoluble aggregates. During the development of the refolding method, it was found that direct solubilization of the inclusion bodies with Triton X-100 reactivated the enzyme, with a considerable refolding efficiency. About 65% of inclusion body levansucrase was refolded into active levansucrase in the renaturation buffer containing 4% (v/v) Triton X-100. The in vitro refolded enzyme was purified to 95% purity by single-step DEAE-Sepharose ion exchange chromatography. Triton X-100 was removed by this ion exchange chromatography.     

The refolding, purification, and activity analysis of a rice Bowman-Birk inhibitor expressed in Escherichia coli

A putative rice trypsin/chymotrypsin inhibitor of the Bowman-Birk family, RBBI-8 of about 20 kDa, was expressed in Escherichia coli as a fusion protein bearing an N-terminal (His)6 purification tag. The expressed recombinant protein, rRBBI-8, is insoluble and accumulates as inclusion bodies. The insoluble protein was solubilized in 8 M urea under reducing environment and then refolded into its active conformation under optimized redox conditions. Strategies used to optimize yield and efficiency include selecting the redox system, increasing protein concentration during refolding by adding the denatured protein in a stepwise way, utilizing additives to prevent aggregation, and selecting buffer-exchanging conditions. A Ni-chelate affinity column was then employed to purify the renatured protein. rRBBI-8 shows strong inhibitory activity against trypsin and it can slightly inhibit chymotrypsin. In this study, a refolding and purification system was set up for this cysteine-rich recombinant protein expressed in a prokaryotic system.     

Expression, refolding, and purification of active diacetylchitobiose deacetylase from Pyrococcus horikoshii

A chitinase from the hyperthermophilic archaeon Pyrococcus furiosus degrades chitin to produce diacetylchitobiose [(GlcNAc)(2)] as the end product. To further investigate the degradation mechanism of (GlcNAc)(2) in Pyrococcus spp., we cloned the gene of PH0499 from Pyrococcus horikoshii, which encodes a protein homologous to the diacetylchitobiose deacetylase of Thermococcus kodakaraensis. The deacetylase (Ph-Dac) was overexpressed as inclusion bodies in Escherichia coli Rosetta (DE3) pLys. The insoluble inclusion body was solubilized and reactivated through a refolding procedure. After several purification steps, 40 mg of soluble, thermostable (up to 80°C) Ph-Dac was obtained from 1L of culture. The apparent molecular mass of the refolded Ph-Dac was 180 kDa, indicating Ph-Dac to be a homohexamer. The refolded Ph-Dac also exhibited deacetylase activity toward (GlcNAc)(2), and the deacetylation site was revealed to be specific to the nonreducing end residue of (GlcNAc)(2). These expression and purification systems are useful for further characterization of Ph-Dac.     

Cloning, expression, and refolding of a secretory protein ESAT-6 of Mycobacterium tuberculosis

A DNA encoding the 6-kDa early secretory antigenic target (ESAT-6) of Mycobacterium tuberculosis was inserted into a bacterial expression vector of pQE30 resulting in a 6x His-esat-6 fusion gene construction. This plasmid was transformed into Escherichia coli strain M15 and effectively expressed. The expressed fusion protein was found almost entirely in the insoluble form (inclusion bodies) in cell lysate. The inclusion bodies were solubilized with 8M urea or 6M guanidine-hydrochloride at pH 7.4, and the recombinant protein was purified by Ni-NTA column. The purified fusion protein was refolded by dialysis with a gradient of decreasing concentration of urea or guanidine hydrochloride or by the size exclusion protein refolding system. The yield of refolded protein obtained from urea dialysis was 20 times higher than that from guanidine-hydrochloride. Sixty-six percent of recombinant ESAT-6 was successfully refolded as monomer protein by urea gradient dialysis, while 69% of recombinant ESAT-6 was successfully refolded as monomer protein by using Sephadex G-200 size exclusion column. These results indicate that urea is more suitable than guanidine-hydrochloride in extracting and refolding the protein. Between the urea gradient dialysis and the size exclusion protein refolding system, the yield of the monomer protein was almost the same, but the size exclusion protein refolding system needs less time and reagents.     

Refolding and Purification of Zymomonas mobilis Levansucrase Produced as Inclusion Bodies in Fed-Batch Culture of Recombinant Escherichia coli

Zymomonas mobilis levansucrase was overproduced by the fed-batch culture of recombinant Escherichia coli harboring a novel expression system that is constitutively expressed by the promoter from the Rahnella aquatilis levansucrase gene. Most of the levansucrase was produced as inclusion bodies in the bacterial cytoplasm, accounting for approximately 20% of the total cellular protein. Refolding after complete denaturation by high concentrations of urea or guanidine hydrochloride was not successful, resulting in large amounts of insoluble aggregates. During the development of the refolding method, it was found that direct solubilization of the inclusion bodies with Triton X-100 reactivated the enzyme, with a considerable refolding efficiency. About 65% of inclusion body levansucrase was refolded into active levansucrase in the renaturation buffer containing 4% (v/v) Triton X-100. The in vitro refolded enzyme was purified to 95% purity by single-step DEAE–Sepharose ion exchange chromatography. Triton X-100 was removed by this ion exchange chromatography.     

A screening system for the identification of refolding conditions for a model protein kinase, p38alpha

Protein kinases are key drug targets involved in the regulation of a wide variety of cellular processes. To aid the development of drugs targeting these kinases, it is necessary to express recombinant protein in large amounts. The expression of these kinases in Escherichia coli often leads to the accumulation of the expressed protein as insoluble inclusion bodies. The refolding of these inclusion bodies could provide a route to soluble protein, but there is little reported success in this area. We set out to develop a system for the screening of refolding conditions for a model protein kinase, p38α, and applied this system to denatured p38α derived from natively folded and inclusion body protein. Clear differences were observed in the refolding yields obtained, suggesting differences in the folded state of these preparations. Using the screening system, we have established conditions under which soluble, folded p38α can be produced from inclusion bodies. We have shown that the refolding yields obtained in this screen are suitable for the economic large-scale production of refolded p38α protein kinase.     

Purification of truncated and mutated Chemotaxis Inhibitory Protein of Staphylococcus aureus--an anti-inflammatory protein

The Chemotaxis Inhibitory Protein of Staphylococcus aureus (CHIPS) binds and blocks the C5a receptor (C5aR) and formyl-peptide receptor (FPR). This way, CHIPS is a potent inhibitor of the immune cell recruitment associated with inflammation. Truncation of the protein and the introduction of mutations, shifts the expression towards the insoluble fraction of Escherichia coli, whereas the wild-type protein can be solubly expressed. A protocol for expression and tag independent purification of biologically active CHIPS variants has been established to enable further characterization of an improved CHIPS variant, called ADC-1004. The CHIPS variants were purified by washing of E. coli inclusion bodies followed by refolding and gel filtration. New techniques were utilized to optimize the purification process. Expression in inclusion bodies was increased by the use of Ultra Yield^™ flasks and optimal refolding conditions were determined by the use of the iFOLD Refolding System 2^™.The folding and biological activity of the purified proteins were analyzed by circular dichroism (CD) spectroscopy and flow cytometry, respectively, and compared to solubly produced CHIPS_31–113 and wild-type CHIPS_1–121. We show that the CHIPS variants produced in inclusion bodies can be refolded and purified to achieve equal biological activity as solubly produced CHIPS_31–113 and wild-type CHIPS_1–121. The truncation causes minor structural changes while purification from inclusion bodies or the soluble fraction does not further affect the structure.     

Expression, purification, and in vitro refolding of a humanized single-chain Fv antibody against human CTLA4 (CD152)

A human-derived single-chain Fv (scFv) antibody fragment specific against human CTLA4 (CD152) was produced at high level in Escherichia coli. The scFv gene was cloned from a phagemid to the expression vector pQE30 with a N-terminal 6His tag fused in-frame, and expressed as a 29 kDa protein in E. coli as inclusion bodies. The inclusion body of scFv was isolated from E. coli lysate, solubilized in 8M urea with 10mM dithiothreitol, and purified by ion-exchange chromatography. Method for in vitro refolding of the scFv was established. The effects of refolding buffer composition, protein concentration and temperature on the refolding yield were investigated. The protein was renatured finally by dialyzing against 3mM GSH, 1mM GSSG, 150 mM NaCl, 1M urea, and 50 mM Tris-Cl (pH 8.0) for 48 h at 4 degrees C, and then dialyzed against phosphate-buffered saline (pH 7.4) to remove remaining denaturant. This refolding protocol generated up to a 70% yield of soluble protein. Soluble scFv was characterized for its specific antigen-binding activity by indirect cellular ELISA. The refolded scFv was functionally active and was able to bind specifically to CTLA4 (CD152). The epitopes recognized by refolded anti-CTLA4 scFv do not coincide with those epitopes recognized by CD80/CD86.