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.     

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.     

Refolding and purification of non-fusion HPT protein expressed in Escherichia coli as inclusion bodies

The gene encoding hygromycin B phosphotransferase (hpt) is a widely used selectable marker in the production of genetically engineered crops. To facilitate the safety assessment of this protein, the non-fusion hpt expression plasmid was constructed and introduced into Escherichia coli to produce enough quantity of the HPT protein. High level expressed HPT was achieved but most of the expressed protein aggregated as inclusion bodies. The inclusion bodies were washed, separated from the cells, and solubilized by 0.3% Sarkosyl. The protein was renatured by dilution and dialysis, and then purified by anion-exchange chromatography. The activity is 8 U/mg protein and the purity is about 95%. Further studies showed that the microbially produced HPT protein had comparable molecular weight, immuno-reactivities, N-terminal amino acid sequences, and biological activities with those of the HPT produced by transgenic rice harboring hpt gene. All these results demonstrated the validity of utilizing the microbially produced HPT to assess the safety of the HPT protein produced in genetically engineered rice.     

Refolding of porcine growth hormone from inclusion bodies of Escherichia coli

Escherichia. coli cells expressing porcine growth hormone were grown in a batch fermentation process. The expression level was estimated to be nearly 40% of the total cellular protein after 2–3 h of induction with 1?mM isopropyl β-d-thiogalactoside. Porcine growth hormone expressed as inclusion bodies was solubilized in 8 M urea. Refolding conditions following a dilution protocol in the presence of β-mercaptoethanol or using a glutathione pair were tested. Reverse phase-HPLC was applied to distinguish oxidized, misfolded and reduced forms of the hormone. A ratio of reduced to oxidized glutathione equal to 2/1 was chosen to avoid the formation of misfolded forms at high protein concentration.     

Refolding and purification of Apo2L/TRAIL produced as inclusion bodies in high-cell-density cultures of recombinant Escherichia coli

As a new member of tumor necrosis factor (TNF) superfamily, TNF-related apoptosis-inducing ligand (Apo2L/TRAIL) was produced mainly as inclusion bodies by recombinant Escherichia coli with a temperature-inducible expression system. High concentrations of both biomass (65 g dry cells l(-1)) and inactive TRAIL (4.8 g l(-1)) were obtained by applying a high-cell-density cultivation procedure. After the inclusion bodies were washed and solubilized. TRAIL refolded when at 1 mg ml(-1) by a simple pulse dilution method with a 35% yield. Renatured TRAIL was purified to electrophoretic homogeneity by one-step immobilized metal affinity chromatography. The purified TRAIL showed strong cytotoxicity activity against human pancreatic 1990 tumor cells, with ED50 about 1.6 microg ml(-1).     

Refolding of G protein alpha subunits from inclusion bodies expressed in Escherichia coli

Heterotrimeric G proteins relay signals from G protein-coupled receptors (GPCRs) to the interior of the cell. The signaling cascades induced by G protein activation control a wide range of cellular processes. The α subunit is believed to determine which G protein couples to each GPCR, and is the primary determinant of the type of signal transmitted. Several members of the G_α family have been expressed in active form in Escherichia coli. However, production levels of these proteins are limited: in most cases only 10% of total G_α protein expressed is active; the rest accumulates in inclusion bodies. Although G_iα has been readily expressed in soluble form (to 10 mg/L), other α subunits are minimally soluble, and many are exclusively expressed to inclusion bodies. Previous efforts to solubilize and refold G_α from inclusion bodies have not been successful. Here we did a thorough study of the characteristics of G_α subunits (human G_iα(1), human G_sα(short), human G_11α and human G_tα(cone)), solubilized and purified from inclusion bodies. We find that we can obtain soluble protein both by on-column and rapid-dilution techniques. Comparison to native, soluble G_iα expressed from E. coli showed that although the refolded G_α subunits were soluble and retained partial α-helicity characteristic of the native, folded G_α subunit, they did not bind GDP or GTP as effectively as native protein. We conclude that the refolded G_iα protein has a native-like secondary structure, but is predominately in a molten globular state.     

Refolding and purification of recombinant human PDE7A expressed in Escherichia coli as inclusion bodies

We have investigated the refolding and purification of the catalytic domain of human 3',5'-cyclic nucleotide phosphodiesterase 7A1 (PDE7A1) expressed in Escherichia coli. A cDNA encoding an N-terminal-truncated PDE7A1(147-482-His) was amplified by RT-PCR from human peripheral blood cells and inserted into the vector pET21-C for bacterial expression of the enzyme fused to a C-terminal His-tag. The PDE was found to be expressed in the form of inclusion bodies which could be refolded to an active enzyme in buffer containing high concentrations of arginine hydrochloride, ethylene glycol, and magnesium chloride at pH 8.5. The PDE7A1(147-482-His) construct could be purified after dialysis and concentration steps by either Zn2+-IDA-Sepharose chromatography or ResourceQ ion-exchange chromatography to homogeneity. In comparison to the metal-chelate column, the ResourceQ purification resulted in a distinctly better yield and enrichment of the protein. Both the Vmax (0.46 micromol. min(-1). mg(-1) ) and the K(m) (0.1 microM) of the purified enzyme were found to be comparable with published data for native or recombinant catalytically active expressed PDE7A1. Using SDS/PAGE, a molecular mass of 39 kDa was determined (theoretical value 38.783 kDa). As known from several other mammalian PDEs, size-exclusion chromatography using refolded PDE7A1(147-482-His) indicated the formation of dimers. The purified enzyme was soluble at concentrations up to 100 microg/ml. A further increase of protein concentration resulted, however, in precipitation of the enzyme.     

Refolding and characterization of rat liver methionine adenosyltransferase from Escherichia coli inclusion bodies

Methionine adenosyltransferase (MAT) catalyzes the synthesis of S-adenosylmethionine, the major methyl donor for transmethylation reactions. Attempts to perform structural studies using rat liver MAT have met with problems because the protein purified from cellular extracts is heterogeneous. Overexpression of the enzyme in Escherichia coli rendered most of the protein as inclusion bodies. These aggregates were purified by specific washes using urea and Triton X-100 and used for refolding. Maximal activity was obtained when chaotropic solubilization included the structural cation Mg(2+), the protein concentration was kept below 0.1 mg/ml, and denaturant removal was carried out in a two-step process, namely, a fast dilution followed by dialysis in the presence of 10 mM DTT or GSH/GSSG redox buffers. Refolding by this procedure generated the oligomeric forms, MAT I and III, which were basically indistinguishable from the purified rat liver forms in secondary structure and catalytic properties.     

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.     

Protein compositional analysis of inclusion bodies produced in recombinant Escherichia coli

Summary Culture conditions favouring the simulataneous formation of soluble protein and inclusion bodies (IBs) were chosen for producing the cytoplasmic protein -galactosidase or the periplasmic protein TEM--lactomase. Soluble and insoluble cell fractions of Escherichia coli producing either -galactosidase or TEM--lactomase were analyzed by one- and two-dimensional gel electrophoresis and subsequent silver staining or immunodection of the recombinant protein. The results show that truncated fragments of the recombinant protein were not present in the soluble cell fraction but accumulate in the IB fraction. The presense of other cellular, non-plasmid-encoded proteins in IB preparations such as the outer membrane proteins OmpF, OmpC, and OmpA or the ribosomal subunit proteins L7/L12 was attributed to co-precipitation of cell-debris-associated components. Protein-folding enzymes were not detected in IB preprations. The specificity of in-vivo protein association in the formation of IBs and its implication on protein purification is discussed. Correspondence to: J. E. Bailey     

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.     

GlycoPEGylation of recombinant therapeutic proteins produced in Escherichia coli

Covalent attachment of polyethylene glycol, PEGylation, has been shown to prolong the half-life and enhance the pharmacodynamics of therapeutic proteins. Current methods for PEGylation, which rely on chemical conjugation through reactive groups on amino acids, often generate isoforms in which PEG is attached at sites that interfere with bioactivity. Here, we present a novel strategy for site-directed PEGylation using glycosyltransferases to attach PEG to O-glycans. The process involves enzymatic GalNAc glycosylation at specific serine and threonine residues in proteins expressed without glycosylation in Escherichia coli, followed by enzymatic transfer of sialic acid conjugated with PEG to the introduced GalNAc residues. The strategy was applied to three therapeutic polypeptides, granulocyte colony stimulating factor (G-CSF), interferon-alpha2b (IFN-alpha2b), and granulocyte/macrophage colony stimulating factor (GM-CSF), which are currently in clinical use.     

Fragments of prochymosin produced in Escherichia coli form insoluble inclusion bodies.

Bovine prochymosin produced in Escherichia coli has been used as a model system to investigate factors which may cause a recombinant protein to accumulate as insoluble inclusion bodies. A series of plasmids was constructed to investigate the effect of deletions within the prochymosin-coding sequence on protein inclusion body formation. The results demonstrated that as much as 70% of the prochymosin-coding sequence could be deleted with no significant reduction in the accumulation of insoluble protein. The smallest deletion product identified (11,000 molecular weight) retained only one cysteine, yet this product still accumulated as an insoluble product in E. coli.     

Recovery of soluble human renin from inclusion bodies produced in recombinant Escherichia coli

Recombinant human renin synthesized in Escherichia coli in the form of inclusion bodies has been recovered in a soluble form without the use of denaturing agents. The renin protein in soluble fractions has been confirmed by Western immunoblotting.     

Refolding and purification of Bothropstoxin-I, a Lys49-phospholipase A2 homologue, expressed as inclusion bodies in Escherichia coli

Hydrolysis of phospholipids by Group II phospholipase A2 enzymes involves a nucleophilic attack on the sn-2 ester bond by the His48 residue and stabilization of the reaction intermediate by a Ca2+ ion cofactor bound to the Asp49 residue in the protein active site region. Bothropstoxin-I (BthTX-I) is a PLA(2) variant present in the venom of the snake Bothrops jararacussu which shows a Asp49 to Lys substitution and which lacks hydrolytic activity yet damages artificial membranes by a noncatalytic Ca2+-independent mechanism. In order to better characterize this unusual mechanism of membrane damage, we have established an expression system for BthTX-I in Escherichia coli. The DNA-coding sequence for BthTX-I was subcloned into the vector pET11-d, and the BthTX-I was expressed as inclusion bodies in E. coli BL21(DE3). The native BthTX-I contains seven disulfide bonds, and a straightforward protocol has been developed to refold the recombinant protein at high protein concentration in the presence of surfactants using a size-exclusion chromatography matrix. After refolding, recovery yields of 2.5% (corresponding to 4-5 mg of refolded recombinant BthTX-I per liter of bacterial culture) were routinely obtained. After refolding, identical fluorescent and circular dichroism spectra were obtained for the recombinant BthTX-I compared to those of the native protein. Furthermore, the native and refolded recombinant protein demonstrated identical membrane-damaging properties as evaluated by measuring the release of an entrapped fluorescent marker from liposomes.     

Refolding of proteins from inclusion bodies: rational design and recipes

The need to develop protein biomanufacturing platforms that can deliver proteins quickly and cost-effectively is ever more pressing. The rapid rate at which genomes can now be sequenced demands efficient protein production platforms for gene function identification. There is a continued need for the biotech industry to deliver new and more effective protein-based drugs to address new diseases. Bacterial production platforms have the advantage of high expression yields, but insoluble expression of many proteins necessitates the development of diverse and optimised refolding-based processes. Strategies employed to eliminate insoluble expression are reviewed, where it is concluded that inclusion bodies are difficult to eliminate for various reasons. Rational design of refolding systems and recipes are therefore needed to expedite production of recombinant proteins. This review article discusses efforts towards rational design of refolding systems and recipes, which can be guided by the development of refolding screening platforms that yield both qualitative and quantitative information on the progression of a given refolding process. The new opportunities presented by light scattering technologies for developing rational protein refolding buffer systems which in turn can be used to develop new process designs armed with better monitoring and controlling functionalities are discussed. The coupling of dynamic and static light scattering methodologies for incorporation into future bioprocess designs to ensure delivery of high-quality refolded proteins at faster rates is also discussed.     

Purification of inclusion bodies using PEG precipitation under denaturing conditions to produce recombinant therapeutic proteins from Escherichia coli

Applied Microbiology and Biotechnology - It has been documented that the purification of inclusion bodies from Escherichia coli by size exclusion chromatography (SEC) may benefit subsequent...