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.     

On-column refolding of an insoluble histidine tag recombinant exopolyphosphatase from Trypanosoma brucei overexpressed in Escherichia coli

An exopolyphosphatase gene has been cloned by polymerase chain reaction (PCR) from Trypanosoma brucei and the corresponding protein overexpressed as a recombinant His-tag (histidine tag) exopolyphosphatase in E. coli in order to characterize its biochemical activity and to produce antibody to determine its localization. Because overexpression of this protein in bacteria resulted in the formation of inactive inclusion bodies, these structures were first solubilized in denaturant condition (6 M urea). Secondly, after a capture step using immobilized metal affinity chromatography (IMAC), a gradual refolding of the protein was performed on-column from 6 M to 0 M urea in the presence of 1% Triton X-100. Triton X-100 was used to abolish protein aggregation during the refolding step. The purified enzyme was active, demonstrating that at least part of the proteins was properly refolded.     

Immobilized Triton X-100-assisted refolding of Green Fluorescent Protein-Tobacco Etch Virus protease fusion protein using β-cyclodextrin as the eluent

A new protein refolding technique based on the use of the non-charged detergent Triton X-100 immobilized to the cross-linked agarose gel Sepharose High Performance has been developed. The new solid phase was used in combination with soluble β-cyclodextrin (β-CD) to refold recombinant Green Fluorescent Protein fused to Tobacco Etch Virus protease (GFPTEVP) expressed as inclusion bodies in E. coli. Previous attempts to refold recombinant GFPTEVP by dilution had failed. In the new procedure a column packed with Triton X-100-coupled Sepharose High Performance was used to capture unfolded GFPTEVP followed by elution using an increasing β-CD concentration gradient. The yield of properly refolded GFPTEVP was 46% at a protein concentration of 380 μg/ml. In contrast, dilution refolding of GFPTEVP at 200 μg/ml refolding buffer resulted in only 4.7% of native protein.     

融合牛肠激酶轻链EKL包涵体蛋白的复性纯化

大肠杆菌高密度发酵表达肠激酶轻链融合蛋白DsbA-rEKL,主要以包涵体形式存在。包涵体经4mol/L尿素和0.5%TritonX-100洗涤,以6mol/L盐酸胍、100mmol/LDTT溶解,在胱氨酸存在下,以脉冲加样方式复性。融合蛋白复性在6mmol/L胱氨酸存在下、脉冲加量0.03mg/mL和复性终蛋白浓度0.3mg/mL为最佳复性方案。复性的融合蛋白加2mmol/LCaCL2后快速自切。经IDA-Sepharose及Q-Sepharose纯化,rEKL纯度可达95%以上,可高效酶切重组瑞特普酶融合蛋白Trx-rPA。实现了大规模生产rEKL,每升发酵液经复性及纯化后,可得rEKL60mg/L以上,使以融合蛋白表达rPA等药用蛋白成为现实。     

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.     

A Combined Refolding Technique for Recombinant Human Interferon-γ Inclusion Bodies by Ion-exchange Chromatography with a Urea Gradient

Summary A refolding strategy was described for on-column refolding of recombinant human interferon-γ (rhIFN-γ) inclusion bodies by ion-exchange chromatography (IEC). The rhIFN-γ was expressed in E. colias inclusion bodies. Triton X-100 was used first to wash the rhIFN-γ inclusion bodies before chromatographic refolding. The refolding process was performed by gradually decreasing the concentration of urea in the column after the denatured rhIFN-γ protein had bound onto the ion-exchange gel SP-Sepharose Fast Flow. The refolding and purification process for the denatured rhIFN-γ was carried through simultaneously and the purity of the refolded rhIFN-γ was up to 95%. The effects of protein loading, flow rate, urea gradient length and final urea concentration on the refolding were investigated in detail. Under the optimum conditions, the specific activity of rhIFN-γ was up to 7.5 × 10⁵ IU mg⁻¹and active protein recovery was up to 54%.     

Refolding of the Fusion Protein of Recombinant Enterokinase Light Chain rEKL

The fusion protein of enterokinase light chain, DsbA-rEK_L, was expressed mainly in the inclusion body in E. coli. The recombinant bacteria were fermented to high density, with high expression of the fusion protein. After being washed with 0.5 % Triton X-100 and 4 mol/L urea, the inclusion body was dissolved in 6 mol/L guanidine and 100 mmol/L DTT, derivatized by cystine and refolded by pulse refolding. The strategy of pulse refolding involved the addition of 0.03 mg/mL of fusion protein until its final concentration reached 0.3 mg/mL. The refolded protein was autocleaved, and the active EK_L molecule was released after the addition of 2 mmol/L of CaCl₂. Using the two-step purification processes of IDA-Sepharose chromatography and Q-Sepharose chromatography, the purity of rEK_L was found to be above 95 %, with a high activity to cleave the recombinant reteplase fusion protein, Trx-rPA. The yield of purified rEK_L was more than 60 mg/L of cultures. As a result, the therapeutic proteins like rPA could be produced on a large scale in a way such as expressed in the form of fusion proteins.     

Extraction and partial purification of mouse uterine alkaline phosphatase.

Alkaline phosphatase in uterine homogenates from day 7 pregnant mice was solubilized using 0.2% (v/v) Triton X-100 and extracted wtih 20% (v/v) n-butanol. The procedure, which resulted in 182-fold purification, included ammonium sulfate precipitation, DEAE-cellulose anion exchange chromatography and Sephadex G200 gel filtration. Solubilization with Triton X-100 was an important step in the procedure since extraction with n-butanol alone only partially solubilized the enzyme and gave low extraction yields, much of the enzyme activity remaining in association with negatively charged residues. However, butanol extraction of Triton X-100-treated homogenates gave high yields of enzyme and eliminated p-nitrophenyl phosphatases which displayed activity in the pH range 3.0--7.5, together with a large proportion of inactive protein. The activity of the purified enzyme preparations was electrophoretically homogeneous on cellulose acetate membranes, suggesting that the alkaline phosphatase in the mouse uterus exists in a single isozymic form. Polyacrylamide-gel electrophoresis revealed that the purified preparations contained at least one protein as an impurity. Attempts to further purify the alkaline phosphatase by isoelectric focusing were unsuccessful since the enzyme was found to have an isoelectric point of about 5.0 and at this pH it was rapidly inactivated.     

High throughput purification of recombinant human growth hormone using radial flow chromatography

Recombinant human growth hormone (r-hGH) was expressed in Escherichia coli as inclusion bodies. Using fed-batch fermentation process, around 670 mg/L of r-hGH was produced at a cell OD600 of 35. Cell lysis followed by detergent washing resulted in semi-purified inclusion bodies with more than 80% purity. Purified inclusion bodies were homogenous in preparation having an average size of 0.6 μm. Inclusion bodies were solubilized at pH 12 in presence of 2 M urea and refolded by pulsatile dilution. Refolded protein was purified with DEAE-anion exchange chromatography using both radial and axial flow column (50 ml bed volume each). Higher buffer flow rate (30 ml/min) in radial flow column helped in reducing the batch processing time for purification of refolded r-hGH. Radial column based purification resulted in high throughput recovery of diluted refolded r-hGH in comparison to axial column. More than 40% of inclusion body protein could be refolded into bioactive form using the above method in a single batch. Purified r-hGH was analyzed by mass spectroscopy and found to be bioactive by Nb2 cell line proliferation assay. Inclusion body enrichment, mild solubilization, pulsatile refolding and radial flow chromatography worked co-operatively to improve the overall recovery of bioactive protein from inclusion bodies.     

Expression of Torpedo californica creatine kinase in Escherichia coli and purification from inclusion bodies

The pET17 expression vector was used to express creatine kinase from the electric organ of Torpedo californica as inclusion bodies in Escherichia coli BL21(DE3) cells. The insoluble aggregate was dissolved in 8M urea and, following extraction with Triton X-100, the enzyme was refolded by dialysis against Tris buffer (pH 8.0) containing 0.2M NaCl. After two buffer changes, chromatography on Blue Sepharose was used as a final step in the purification procedure. Approximately 54mg active protein was recovered from a 1L culture and the refolded enzyme had a specific activity of 75U/mg. The molecular mass of the purified protein was consistent with that predicted from the amino acid sequence and the CD spectrum of the refolded enzyme was essentially identical to that of creatine kinase from human muscle (HMCK). The K(m) values of ATP and ADP were also similar to those of HMCK, while the K(m) values for both phosphocreatine and creatine were approximately 5-10-fold higher. The purification described here is in marked contrast with earlier attempts at purification of this isozyme where, in a process yielding less than 1mg/L culture, enzyme with a specific activity of ca. 5U/mg was obtained.     

Activity of maize transglutaminase overexpressed in Escherichia coli inclusion bodies: an alternative to protein refolding

Transglutaminases (TGases) catalyze protein post-translational modification by ε-(γ-glutamyl) links and covalent polyamine conjugation. In plants, this enzyme is poorly characterized and only the maize plastidial TGase gene (tgz) has been cloned. The tgz gene (Patent WWO03102128) had been subcloned and overexpressed in Escherichia coli cells, and the recombinant protein (TGZp) was present mainly in inclusion bodies (IB) fraction. In this work, after overexpression of TGZ15p and SDS-PAGE IB fraction analysis, bands about 65 and 56 kDa were obtained. Western blot, alkylation and MALDI-TOF/TOF analyses indicated that the 56 kDa band corresponded to a truncated sequence from the native TGZ15p (expected MW 65 kDa), by elimination of a chloroplast signal peptide fragment during expression processing. So that large-scale protein production and protein crystallization can be applied, we characterized the TGZ15p enzyme activity in the IB protein fraction, with and without refolding. Results indicate that it presented the biochemical characteristics of other described TGases, showing a certain plant-substrate preference. Solubilization of the IB fraction with Triton X-100 as nondenaturing detergent yielded active TGZ without the need for refolding, giving activity values comparable to those of the refolded protein, indicating that this is a valuable, faster way to obtain TGZ active protein.     

一种新型广谱流感病毒亚单位疫苗的表达与纯化

通过引物设计,利用重叠延伸PCR（OE-PCR）和搭桥PCR方法扩增得到A型流感病毒M2蛋白缺失跨膜区基因以及HA多表位基因,分别克隆测序后以pET28a+为表达载体构建重组质粒pET28a+-M2d-HA。将重组质粒转化大肠杆菌BL21（DE3）,筛选获得了高效表达流感病毒缺失跨膜区M2蛋白和HA多表位蛋白片段重组融合蛋白的工程菌,表达的重组蛋白约占菌体总蛋白总量的45%左右。表达的蛋白以包涵体形式存在,包涵体经亲和层析和阴离子交换层析纯化后复性,得到纯度在90%以上的目的蛋白。Western blot结果显示纯化的重组蛋白具有较好的抗原性和特异性。此项工作为进一步研究广谱型流感病毒亚单位疫苗奠定了基础。     

Effects of solutes on solubilization and refolding of proteins from inclusion bodies with high hydrostatic pressure

High hydrostatic pressure (HHP)-mediated solubilization and refolding of five inclusion bodies (IBs) produced from bacteria, three gram-negative binding proteins (GNBP1, GNBP2, and GNBP3) from Drosophila, and two phosphatases from human were investigated in combination of a redox-shuffling agent (2 mM DTT and 6 mM GSSG) and various additives. HHP (200 MPa) combined with the redox-shuffling agent resulted in solubilization yields of approximately 42%-58% from 1 mg/mL of IBs. Addition of urea (1 and 2 M), 2.5 M glycerol, L-arginine (0.5 M), Tween 20 (0.1 mM), or Triton X-100 (0.5 mM) significantly enhanced the solubilization yield for all proteins. However, urea, glycerol, and nonionic surfactants populated more soluble oligomeric species than monomeric species, whereas arginine dominantly induced functional monomeric species (approximately 70%-100%) to achieve refolding yields of approximately 55%-78% from IBs (1 mg/mL). Our results suggest that the combination of HHP with arginine is most effective in enhancing the refolding yield by preventing aggregation of partially folded intermediates populated during the refolding. Using the refolded proteins, the binding specificity of GNBP2 and GNBP3 was newly identified the same as with that of GNBP1, and the enzymatic activities of the two phosphatases facilitates their further characterization.     

Refolding,purification and characterization of an organic solvent-tolerant lipase from Serratia marcescens ECU1010

Expression of recombinant proteins as inclusion bodies in bacteria is one of the most efficient ways to produce cloned proteins, as long as the inclusion bodies can be successfully refolded. In this study, the different parameters were investigated and optimized on the refolding of denatured lipase. The maximum lipase activity of 5000 U/L was obtained after incubation of denatured enzyme in a refolding buffer containing 20 mM Tris–HCl (pH 7.0), 1 mM Ca²⁺ at 20 °C. Then, the refolded lipase was purified to homogeneity by anion exchange chromatography. The purified refolded lipase was stable in broad ranges of temperatures and pH values, as well as in a series of water-miscible organic solvents. In addition, some water-immiscible organic solvents, such as petroleum ether and isopropyl ether, could reduce the polarity and increase the nonpolarity of the refolding system. The results of Fourier transform infrared (FT-IR) microspectroscopy were the first to confirm that lipase refolding could be further improved in the presence of organic solvents. The purified refolded lipase could enantioselectively hydrolyze trans-3-(4-methoxyphenyl) glycidic acid methyl ester [(±)-MPGM]. These features render the lipase attraction for biotechnological applications in the field of organic synthesis and pharmaceutical industry.     

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     

huGM-CSF(9-127)-IL-6(29-184)融合蛋白的复性及纯化研究

利用Q Sepharose H.P.离子交换柱层析在8mol/L尿素变性条件下对huGM-CSF(9-127)-IL-6(29-184）融合蛋白进行初步纯化,然后再利用Sephacryl S-200分子筛柱层析复性及纯化后获得目的蛋白,其纯度达到95％以上。该纯化方案成功地解决了稀释复性或透析复性产物在进行Q Sepharose H.P.离子交换柱层析时目的蛋白不稳定而沉积于柱上的问题,获得了较好的复性效果,复性率达到80％以上。使用该纯化方案,1天内便可基本完成重组蛋白的复性及纯化过程,而且也便于扩大。     

Renaturation of cobra venom phospholipase A2 expressed from a synthetic gene in Escherichia coli.

Cobra venom (Naja naja naja) phospholipase A2 (PLA2) contains 14 cysteines in the form of 7 disulfide bonds amongst its 119 amino acids. A gene encoding the PLA2 was synthesized and inserted into a bacterial expression vector containing the phage lambda pL promoter. In order to obtain protein without the initiating methionine at the N-terminus, a Factor Xa site was engineered upstream from the PLA2 gene. Upon heat-induction of the cells transformed with the expression plasmid, the protein is produced as insoluble inclusion bodies. The enzyme was partially purified by washing the inclusion bodies with Triton X-100 and urea. The expressed protein was first denatured with 8 M guanidine-HCl and 10 mM DTT. After digestion with Factor Xa, formation of disulfide bonds and refolding into the fully active form was carried out in the presence of cysteine and Ca2+. The renatured recombinant protein was purified by Affi-gel blue column chromatography. The purified recombinant enzyme had the same specific activity as the native enzyme when assayed on a variety of substrates and cross-reacted with antisera prepared against the native enzyme. This is the first report of the expression of a recombinant PLA2 from any venom.     

Expression, purification, and refolding of biologically active Acinetobacter baumannii OmpA from Escherichia coli inclusion bodies

Infections caused by Acinetobacter baumannii have emerged as a significant clinical problem due to the increase in infections caused by antibiotic resistant strains. A. baumannii OmpA is a highly conserved membrane protein that has multiple roles in interacting with the host during infection, and thus represents an attractive target for the development of novel antibacterial therapies. In the present study, the coding sequence of the mature form of A. baumannii OmpA was cloned into the vector pET-15b and purified under denaturing conditions from Escherichia coli inclusion bodies using nickel affinity chromatography. A Triton X-114 wash step was incorporated into the purification method in order to remove endotoxin, resulting in endotoxin levels of <1.3 EU/mg of protein. A protocol was developed for refolding the purified protein by dilution into the non-ionic detergent n-octyl-β-D-glucopyranoside followed by dialysis to remove excess denaturant and detergent. Cytotoxicity assays demonstrated that refolded A. baumannii OmpA was able to induce cell death in A549 cells. In addition, a polyclonal antibody was raised against the refolded protein and used to assess extracellular secretion of OmpA by Western blot. This protein expression and purification system may be useful for further characterization of A. baumannii OmpA.     

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     

Solubilization and partial purification of an enzyme involved in rat liver microsomal fatty acid chain elongation: beta-hydroxyacyl-CoA dehydrase.

The solubilization and partial purification of beta-hydroxyacyl-CoA dehydrase from rat liver microsomes has been accomplished through deoxycholate solubilization, ammonium sulfate fractionation, and ion exchange chromatography. A purification of about 90-fold based on total soluble activity was achieved, with an overall yield of 40%. However, the initial solubilization is accompanied by the loss of the secondary portion of the v/s curve observed with intact microsomes. The enzyme requires detergent during the purification procedure to remain "soluble," and is strongly activated by the inclusion of Triton-X-100 at concentrations above its critical micelle concentration in the assay mixture. In addition a preference for micelles has been inferred based on discontinuities in the v/s curves relative to the measured critical micelle concentration of the substrates in the absence of Triton X-100. Kinetic parameters calculated on the basis of micelle-specific activity indicated that beta-hydroxyacyl-CoA substrates possessing even-numbered alkyl chains from 14 to 20 carbon atoms differed little in Vm', but had progressively larger Km' as the chain length increased. The partially purified preparation was also active with beta-hydroxy-8,11-eicosadienoyl-CoA; and with 2-trans-enoyl-CoA substrates in a reverse (hydration) reaction.