Effect of biosynthetic manipulation of heme on insolubility of Vitreoscilla hemoglobin in Escherichia coli.

Vitreoscilla hemoglobin (VHb) is accumulated at high levels in both soluble and insoluble forms when expressed from its native promoter on a pUC19-derived plasmid in Escherichia coli. Examination by atomic absorption spectroscopy and electron paramagnetic resonance spectroscopy revealed that the insoluble form uniformly lacks the heme prosthetic group (apoVHb). The purified soluble form contains heme (holoVHb) and is spectroscopically indistinguishable from holoVHb produced by Vitreoscilla cells. This observation suggested that a relationship may exist between the insolubility of apoVHb and biosynthesis of heme. To examine this possibility, a series of experiments were conducted to chemically and genetically manipulate the formation and conversion of 5-aminolevulinic acid (ALA), a key intermediate in heme biosynthesis. Chemical perturbations involved supplementing the growth medium with the intermediate ALA and the competitive inhibitor levulinic acid which freely cross the cell barrier. Genetic manipulations involved amplifying the gene dosage for the enzymes ALA synthase and ALA dehydratase. Results from both levulinic acid and ALA supplementations indicate that the level of soluble holoVHb correlates with the heme level but that the level of insoluble apoVHb does not. The ratio of soluble to insoluble VHb also does not correlate with the level of total VHb accumulated. The effect of amplifying ALA synthase and ALA dehydratase gene dosage is complex and may involve secondary factors. Results indicate that the rate-limiting step of heme biosynthesis in cells overproducing VHb does not lie at ALA synthesis, as it reportedly does in wild-type E. coli (S. Hino and A. Ishida, Enzyme 16:42-49, 1973).     

Employment of colorimetric enzyme assay for monitoring expression and solubility of GST fusion proteins targeted to inclusion bodies

High levels of recombinant protein expression can lead to the formation of insoluble inclusion bodies. These complex aggregates are commonly solubilized in strong denaturants, such as 6–8 M urea, although, if possible, solubilization under milder conditions could facilitate subsequent refolding and purification of bioactive proteins. Commercially available GST-tag assays are designed for quantitative measurement of GST activity under native conditions. GST fusion proteins accumulated in inclusion bodies are considered to be undetectable by such assays. In this work, solubilization of recombinantly produced proteins was performed in 4 M urea. The activity of rGST was assayed in 2 M urea and it was shown that rGST preserves 85% of its activity under such denaturing conditions. A colorimetric GST activity assay with 1-chloro-2, 4-dinitrobenzene (CDNB) was examined for use in rapid detection of expression targeted to inclusion bodies and for the identification of inclusion body proteins which can be solubilized in low concentrations of chaotropic agents. Applicability of the assay was evaluated by tracking protein expression of two GST-fused allergens of biopharmaceutical value in E. coli, GST-Der p 2 and GST-Mus a 5, both targeted to inclusion bodies.     

HIV-1 Gag蛋白在大肠杆菌表达系统中诱导和纯化条件的优化

为探讨诱导温度对于HIV-1 Gag在大肠杆菌中表达产物状态以及尿素浓度对蛋白纯化效果的影响, 将30oC和37oC诱导表达的包涵体分别溶于不同浓度的尿素, 比较溶解性的差异, 并比较复性的不同。将30oC诱导的目的蛋白分别用2 mol/L和8 mol/L尿素溶解后做层析分离, 比较两者的分离效果。结果发现, 与37oC相比, 30oC诱导表达的蛋白能有效溶于低浓度尿素, 并且更容易复性。与8 mol/L尿素溶解相比, 30oC诱导的包涵体用2 mol/L尿素溶解后通过凝胶过滤和离子交换层析纯化能得到更好的分离效果。这提示低温诱导的Gag包涵体中可能含有更多类似天然态构象的蛋白, 而低浓度尿素有利于保持包涵体中蛋白的天然态构象。从而为包涵体蛋白的诱导表达和分离纯化提供了参考。     

Analysis of the disulfide bonding pattern between domain sequences of recombinant prochymosin solubilized from inclusion bodies

Prochymosin contains three disulfide bonds linking Cys45 to Cys50, Cys206 to Cys210, and Cys250 to Cys283. To analyze the disulfide bonding pattern between domain sequences in the recombinant prochymosin molecule solubilized from inclusion bodies by 8 M urea (designated as solubilized prochymosin), a simple peptide mapping method was established. This process consists of thiol alkylation, cleavage with cyanogen bromide, diagonal electrophoresis on polyacrylamide gel, and N-terminal sequencing. By using this procedure it was found that Cys45 and Cys50 located in the N-terminal domain are not mispaired with the cysteine residues, located in the C-terminal domain, in the solubilized wild-type prochymosin and its mutants. This result implies that Cys45 and Cys50, the partners of a native disulfide, are restricted in some ordered structures existing in inclusion bodies and remaining after solubilization. These native structural elements act as folding nuclei to initiate and facilitate correct refolding. The strategy of preserving the native-like structures including native disulfide in the solubilized inclusion bodies to enhance renaturation efficiency may be applicable to other recombinant proteins.Both authors contributed equally to this work     

Improved solubilization of recombinant human growth hormone inclusion body produced in Escherichia coli

Recombinant human growth hormone (r-hGH) overexpressed in Escherichia coli forms inactive and insoluble aggregates as inclusion bodies in the cytoplasm. The efficient solubilization of inclusion bodies is critical for cost-effective production. Contrary to a previous report, in our production system, the solubilization method by alkaline treatment including 2 M urea was ineffective. Hence various buffers containing different concentrations of urea or guanidine hydrochloride (GnHCl) at neutral and alkaline pH were attempted. Efficient solubilization (about 90%) was observed in 100 mM Tris buffer, pH 8.0, with more than 4 M GnHCl, and at pH 12.5 with more than 2 M GnHCl, but not with about 8 M of urea. The r-hGH solubilized at pH 12.5 containing 2 M GnHCl was refolded by simple dilution and purified by DEAE Sepharose anion-exchange chromatography. The biological activity of the resulting r-hGH was comparable with commercially available r-hGH in in vitro cell proliferation assay using the hGH-dependent cell line.     

Thermolabile antifreeze protein produced in Escherichia coli for structural analysis

Inclusion bodies of recombinant human growth hormone (r-hGH) were isolated from Escherichia coli, enriched and solubilized in 100 mM Tris buffer containing 6 M n-propanol and 2 M urea. Around 4 mg/ml of r-hGH from inclusion bodies were solubilized in 6 M n-propanol-based buffer containing 2 M urea. Existence of native-like secondary structure of r-hGH in 6 M n-propanol solution was confirmed by CD and fluorescence spectra. Solubilized r-hGH was subsequently refolded by pulsatile dilution, purified to homogeneity and found to be functionally active. Tris buffer containing 6 M n-propanol and 2 M urea also effectively solubilized a number of proteins expressed as inclusion bodies in E. coli. Mild solubilization of inclusion body proteins, chaotropic effect of n-propanol at high concentration and kosmotropic effect at lower concentration helped in improved refolding of the solubilized protein. Around 40% of the r-hGH in the form of inclusion body aggregates was refolded into bioactive form while using n-propanol as solubilization agent. Solubilization with 6 M n-propanol solution thus can be a viable alternative for achieving high throughput recovery of bioactive protein from inclusion bodies of E. coli.     

Optimized procedures for purification and solubilization of basic fibroblast growth factor inclusion bodies

The efficiency of purification of basic fibroblast growth factor (bFGF) inclusion bodies using EDTA and nonionic detergents was improved from 25 to 40% by shifting the pH from 8.5 to strong alkaline conditions (pH 9.5 – 10.5). Complete dissolution of bFGF inclusion bodies by guanidinium hydrochloride (> 3 m) was independent of pH and the presence of reducing agents. In contrast, solubilization of bFGF inclusion bodies by urea was pH-dependent and increased in efficiency (e.g. from 0 to 100%) by increasing the pH (from pH 5.0 to 10.5 at 9 m urea). The purification and solubilization procedures are efficient for inclusion body concentrations corresponding to 10 and 100 g per l dry cell weight, respectively.     

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.     

Renaturation of recombinant proteins produced as inclusion bodies

Expression of recombinant proteins in Escherichia coli often results in the formation of insoluble inclusion bodies. Within the last few years specific methods and strategies have been developed to prepare active proteins from these inclusion bodies. These methods include (i) isolation of inclusion bodies after disintegration of cells by mechanical forces and purification by washing with detergent solutions or low concentrations of denaturant, (ii) solubilization of inclusion bodies with high concentrations of urea or guanidine-hydrochloride in combination with reducing reagents, and (iii) renaturation of the proteins including formation of native disulphide bonds. Renatured and native disulphide bond formation are accomplished by (a) either air oxidation, (b) glutathione reoxidation starting from reduced material, or (c) disulphide interchange starting from mixed disulphides containing peptides. The final yield of renatured proteins can be increased by adding low concentrations of denaturant during renaturation.     

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

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

Structural characteristics and refolding of in vivo aggregated hyperthermophilic archaeon proteins

Several recombinant proteins in inclusion bodies expressed in Escherichia coli have been measured by Fourier transform infrared and solid-state nuclear magnetic resonance spectra to provide the secondary structural characteristics of the proteins from hyperthermophilic archaeon Pyrococcus horikoshii OT3 (hyperthermophilic proteins) in inclusion bodies. The beta-strand-rich single chain Fv fragment (scFv) and alpha-helix-rich interleukin (IL)-4 lost part of the native-like secondary structure in inclusion bodies, while the inclusion bodies composed of the hyperthermophilic proteins of which the native form is alpha-helix rich, are predominated by alpha-helix structure. Further, the secondary structure of the recombinant proteins solubilized from inclusion bodies by detergent or denaturant was observed by circular dichroism (CD) spectra. The solubilization induced the denaturation of the secondary structure for scFv and IL-4, whereas the solubilized hyperthermophilic proteins have retained the alpha-helix structure with the CD properties resembling those of their native forms. This indicates that the hyperthermophilic proteins form native-like secondary structure in inclusion bodies. Refolding of several hyperthermophilic proteins from in vivo aggregated form without complete denaturation could be accomplished by solubilization with lower concentration (e.g. 2 M) of guanidine hydrochloride and removal of the denaturant via stepwise dialysis. This supports the existence of proteins with native-like structure in inclusion bodies and suggests that non-native association between the secondary structure elements leads to in vivo aggregation. We propose a refolding procedure on the basis of the structural properties of the aggregated archaeon proteins.     

Expression, purification, and refolding of a novel immunotoxin containing humanized single-chain fragment variable antibody against CTLA4 and the N-terminal fragment of human perforin

Immunotoxins might be potential in treatment of cancer for their ability to kill selected cell populations. We constructed a novel immunotoxin hS83P34 by fusing N-terminal 34 amino acid fragment of human perforin to the C-terminus of humanized single-chain fragment variable antibody against CTLA4. The fusion protein was inductively expressed as inclusion bodies at a high level about 30% of total bacterial proteins. After washing with buffer containing 2 M urea, the purity of inclusion body was about 71%. The washed inclusion bodies were solubilized in 8 M urea and further purified to homogeneity (approximately 92% purity) by cation-exchange chromatography and Ni-agarose affinity chromatography under denaturing condition. The inclusion body refolding conditions were optimized following Pro-Matrix Protein Refolding Guide. After refolded in Tris buffer (pH 8.0) containing 1M urea, 0.8 M l-arginine, and 2 mM GSH:0.2 mM GSSG or 2 mM GSH:0.4 mM GSSG for 18h at 4 degrees C, over 90% proteins were recovered from inclusion bodies. In vitro dose-dependent cytotoxicity assay demonstrates that hS83P34 is only toxic to CTLA4-positive cells. IC(50) of hS83P34 for leukemic cells Raji and 6T-CEM are about 0.85 and 1.3 microM individually. Whereas, CTLA4-negative endothelial cell ECV-304 is resistant to hS83P34.     

Recovery of active N-acetyl-D-glucosamine 2-epimerase from inclusion bodies by solubilization with non-denaturing buffers

Overexpression of recombinant N-acetyl-d-glucosamine 2-epimerase, one of the key enzymes for the synthesis of N-acetylneuraminic acid, in E. coli led to the formation of protein inclusion bodies. In this study we report the recovery of active epimerase from inclusion bodies by direct solubilization with Tris buffer. At pH 7.0, 25% of the inclusion bodies were solubilized with Tris buffer. The specific activity of the solubilized proteins, 2.08 ± 0.02 U/mg, was similar to that of the native protein, 2.13 ± 0.01 U/mg. The result of circular dichroism spectroscopy analysis indicated that the structure of the solubilized epimerase obtained with pH 7.0 Tris buffer was similar to that of the native epimerase purified from the clarified cell lysate. As expected, the extent of deviation in CD spectra increased with buffer pH. The total enzyme activity recovered by solubilization from inclusion bodies, 170.41 ± 10.06 U/l, was more than 2.5 times higher than that from the clarified cell lysate, 67.32 ± 5.53 U/l. The results reported in this study confirm the hypothesis that the aggregation of proteins into inclusion bodies is reversible and suggest that direct solubilization with non-denaturing buffers is a promising approach for the recovery of active proteins from inclusion bodies, especially for aggregation-prone multisubunit proteins.     

Protein stabilization by urea and guanidine hydrochloride

The urea, guanidine hydrochloride, salt, and temperature dependence of the rate of dissociation of CO from a nonequilibrium state of CO-bound native ferrocytochrome c has been studied at pH 7. The heme iron of ferrocytochrome c in the presence of denaturing concentrations of guanidine hydrochloride (GdnHCl) and urea prepared in 0.1 M phosphate, pH 7, binds CO. When the unfolded protein solution is diluted 101-fold into CO-free folding buffer, the protein chain refolds completely, leaving the CO molecule bonded to the heme iron. Subsequently, slow thermal dissociation of the CO molecule yields to the heme coordination of the native M80 ligand. Thus, the reaction monitors the rate of thermal conversion of the CO-liganded native ferrocytochrome c to the M80-liganded native protein. The rate of this reaction, k(diss), shows a characteristic dependence on the presence of nondenaturing concentrations of the denaturants in the reaction medium. The rate decreases by approximately 1.9-3-fold as the concentration of GdnHCl in the refolding medium increases from nearly 0 to approximately 2.1 M. Similarly, the rate decreases by 1.8-fold as the urea concentration is raised from 0.l to approximately 5 M. At still higher concentrations of the denaturants the denaturing effect sets in, the protein is destabilized, and hence the CO dissociation rate increases sharply. The activation energy of the reaction, E(a), increases when the denaturant concentration in the reaction medium is raised: from 24.1 to 28.3 kcal mol(-1) for a 0.05-2.1 M rise in GdnHCl and from 25.2 to 26.9 kcal mol(-1) for a 0.1-26.9 M increase in urea. Corresponding to these increases in denaturant concentrations are also increases in the activation entropy, S(diss)/R, where R is the gas constant of the reaction. The denaturant dependence of these kinetic and thermodynamic parameters of the CO dissociation reaction suggests that binding interactions with GdnHCl and urea can increase the structural and energetic stability of ferrocytochrome c up to the limit of the subdenaturing concentrations of the additives. NaCl and Na(2)SO(4), which stabilize proteins through their salting-in effect, also decrease the rate with a corresponding increase in activation entropy of CO dissociation from CO-bound native ferrocytochrome c, lending support to the view that low concentrations of GdnHCl and urea stabilize proteins. These results have direct relevance to the understanding and interpretation of the free energy-denaturant relationship and protein folding chevrons.     

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.     

Isolation, ultrastructure, and protein composition of the flagellar rootlet of Naegleria gruberi

Attached to the basal bodies of Naegleria gruberi flagellates is a striated rootlet or rhizoplast. The rootlet-basal body complex has been isolated by Triton X-100 lysis of deflagellated cells and differential centrifugation through a 25% glycerol medium. Rootlets isolated from mature flagellates are approximately 13 micrometers long but vary from 8 to 15 micrometers in length: they taper at both ends from a maximum width of approximately 0.25 micrometers in the vicinity of the basal bodies. They are highly stable during isolation but can be solubilized by urea, high salt, low pH, or detergent (Sarkosyl). Partial dissociation of rootlets with 1 M urea reveals that they are composed of filaments, approximately 5 nm diameter, associated in a linear fashion to yield the characteristic 21-nm cross-banded appearance. Differential solubilization of rootlets and their associated contaminants allowed identification of a major rootlet protein, comprising at least 50% of any purified rootlet preparation, with an apparent subunit molecular weight of 170,000. The localization of rootlets in situ by indirect immunofluorescence using a specific antibody directed against the purified rootlet protein demonstrated unequivocally that this 170,000-dalton protein is an organelle component.     

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

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

Protein composition of Vitreoscilla hemoglobin inclusion bodies produced in Escherichia coli

The protein composition of inclusion bodies produced in recombinant Escherichia coli overproducing Vitreoscilla hemoglobin (VHb) was analyzed by one-dimensional and two-dimensional electrophoresis techniques. Results indicate the presence of two types of cytoplasmic aggregates of differing morphology in single bacterial cells. These aggregates also differ in their relative content of VHb and pre-beta-lactamase and are separable by differential centrifugation. Results further suggest that the cytoplasmic protein elongation factor Tu is integrated into VHb inclusion bodies. The presence of the outer membrane proteins OmpA and OmpF in inclusion body preparations is attributed to cell envelope contamination rather than specific involvement in inclusion bodies. The specificity of in vivo protein aggregation is discussed.     

Kinetics of inclusion body formation and its correlation with the characteristics of protein aggregates in Escherichia coli

The objective of the research was to understand the structural determinants governing protein aggregation into inclusion bodies during expression of recombinant proteins in Escherichia coli. Recombinant human growth hormone (hGH) and asparaginase were expressed as inclusion bodies in E.coli and the kinetics of aggregate formation was analyzed in details. Asparaginase inclusion bodies were of smaller size (200 nm) and the size of the aggregates did not increase with induction time. In contrast, the seeding and growth behavior of hGH inclusion bodies were found to be sequential, kinetically stable and the aggregate size increased from 200 to 800 nm with induction time. Human growth hormone inclusion bodies showed higher resistance to denaturants and proteinase K degradation in comparison to those of asparaginase inclusion bodies. Asparaginase inclusion bodies were completely solubilized at 2-3 M urea concentration and could be refolded into active protein, whereas 7 M urea was required for complete solubilization of hGH inclusion bodies. Both hGH and asparaginase inclusion bodies showed binding with amyloid specific dyes. In spite of its low β-sheet content, binding with dyes was more prominent in case of hGH inclusion bodies than that of asparaginase. Arrangements of protein molecules present in the surface as well as in the core of inclusion bodies were similar. Hydrophobic interactions between partially folded amphiphillic and hydrophobic alpha-helices were found to be one of the main determinants of hGH inclusion body formation. Aggregation behavior of the protein molecules decides the nature and properties of inclusion bodies.     

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.