Translational features of human alpha 2b interferon production in Escherichia coli

The yield of human alpha 2b interferon in Escherichia coli was optimized by replacement of low-usage arginine codons located in the mRNA 5' end. The differences observed among the various gene variants suggest that codon usage, Shine-Dalgarno-like sequences, and mRNA secondary structure contribute to the performance of E. coli translation machinery.     

Overexpression and purification of recombinant human interferon alpha2b in Escherichia coli

Overexpression of rhIFN-alpha2b was obtained by synthesizing a codon optimized gene for IFN-alpha2b and expressing it in the form of inclusion bodies (IBs) in Escherichia coli. The recombinant plasmid pRSET-IFNalpha, which had the IFN-alpha2b gene under the T7 promoter, was coexpressed with plasmid pGP1-2, which carried the gene for T7 RNA polymerase under the heat inducible lambdaP(L) promoter. This two plasmid expression system was optimized with respect to heat shock time, media, and time of induction in shake flask cultures. This was then scaled up into a bioreactor to get a maximum volumetric product yield of 5.2g/L at a final OD(600) of 67. At this point, the IBs represented approximately 40% of the total cellular protein. This high specific product yields eased the further downstream processing steps and improved product recoveries. The IBs were isolated and purified through ion exchange followed by step refolding to give a final product yield of approximately 3g/L, which is maximum reported in the literature. The bioassay of the refolded protein gave a specific activity of approximately 3 x 10(9)IU/mg protein.     

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.     

Expression in Escherichia coli cells of mutant human interferon alpha2

cDNA library was obtained from mRNA isolated from human leukocytes induced by Newcastle disease virus. Clones containing cDNA for alpha 2-interferons were identified by colony hybridization with two synthetic hexadecanucleotides. One of the positive clones contained a NH2-terminal part of cDNA of human interferon identical to cDNA for IFN-alpha 2. The only difference between these two clones was the Ser-8 leads to Asn-8 substitution in deduced sequenced of mature interferons. This mutant interferon, named alpha 2, was expressed in E. coli and its properties were compared with those of interferon alpha 2.     

Extraction of rIL-2 inclusion bodies from Escherichia coli using cross-flow filtration

A cross-flow membrane filtration process was developed for the recovery of rIL-2 inclusion bodies from homogenized Escherichia coli. The membrane extraction process was comprised of a two-step diafiltration followed by an extraction with 7 M GuHCl and a 40-fold dilution of the solubilized inclusion bodies into 0.01 M Tris-HCl, 0.035 M NaCl, pH 7.9. The first diafiltration was with a 0.03 M Tris-HCl, 5 mM ethylenediaminetetraacetic acid (EDTA), pH 8, followed by a diafiltration with 1.75 M GuHCl. All of the insoluble rIL-2 was retained behind the membrane, whereas a GuHCl wash solubilized approximately 15% of the rIL-2. The membrane process increased the yield of rIL-2 in the diluted extract by threefold as compared to a similar centrifuge process with a significant increase in purity as determined by reverse-phase high-performance liquid chromatography (HPLC). (c) 1994 John Wiley & Sons, Inc.     

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 recovery of recombinant human matrix metalloproteinase 7 (matrilysin) from inclusion bodies expressed by Escherichia coli.

The recombinant prepro-form of human matrix metalloproteinase 7 (matrilysin or MMP-7) was overexpressed in Escherichia coli as insoluble inclusion bodies. The recombinant protein was refolded by 100-fold dilution after solubilization with 6 M guanidine HCl. The refolding was monitored by the recovery of matrilysin activity. The addition of either 1.0 M arginine or 0.1% Brij-35 promoted remarkably the refolding. The refolding was dependent on pH and temperature, with lower temperature (<10 degrees C) and pH 6-8 preferable. Glutathione had no effect on refolding, and it was excluded from the refolding conditions. Starting with inclusion bodies (2.0 g, wet) containing 360 mg protein, 29.5 mg of pro-matrilysin (30 kDa) was obtained after refolding with 1.0% Brij-35 at pH 7.5 and 4 degrees C for 12 h. Pro-matrilysin (24.0 mg) was purified to homogeneity by cation-exchange HPLC with a 15-fold increase in purity and an activity yield of 81.3%. Pro-matrilysin was converted entirely to matrilysin (19.0 kDa; 15.2 mg) by activation with a mercuric reagent. The activity (k(cat)/K(m)) of matrilysin was 1.7 x 10(5) M(-1) x s(-1).     

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.     

The pro-sequence facilitates folding of human nerve growth factor from Escherichia coli inclusion bodies.

Nerve growth factor (beta-NGF), a neurotrophin required for the development and survival of specific neuronal populations, is translated as a prepro-protein in vivo. While the presequence mediates translocation into the endoplasmic reticulum, the function of the pro-peptide is so far unknown. As the pro-sequences of several proteins are known to promote folding of the mature part, the renaturation behaviour of recombinant human beta-NGF pro-protein was compared to that of the mature form. Expression of rh-pro-NGF in Escherichia coli led to the formation of inclusion bodies (IBs). The presence of the covalently attached pro-sequence significantly increased the yield and rate of refolding with concomitant disulfide bond formation when compared to the in vitro refolding of mature NGF (rh-NGF). Physicochemical characterization revealed that rh-pro-NGF is a dimer. The pro-peptide could be removed by limited proteolysis with trypsin yielding biologically active, mature rh-NGF. Furthermore, rh-pro-NGF exhibited biological activity in the same concentration range as rh-NGF.     

Periplasmic expression and recovery of human interferon gamma in Escherichia coli

A synthetic human interferon gamma (hIFN-gamma) gene was fused to SP1 and SP3, two Sec-dependent artificial signal peptides to transport the hIFN-gamma to the periplasm of Escherichia coli BL21-SI. The processing efficiency of both SP1-hIFN-gamma and SP3-hIFN-gamma was dependent on the culture medium as well as the post-induction temperature. Both precursors were processed completely when cells were cultured using minimal medium and a post-induction temperature of 32.5 degrees C, and only the processed hIFN-gamma was detected. The SP3 signal peptide was more efficient than SP1 for the secretion of hIFN-gamma. Sixty percent of the total hIFN-gamma was secreted to the periplasm using the SP3 signal peptide and a post-induction temperature of 20 degrees C. Using Tris-sucrose-dithiothreitol (TSD) hypertonic buffer, the periplasmic soluble hINF-gamma was recovered with a purity of 85%.     

The production of human papillomavirus type 16 L1 vaccine product from Escherichia coli inclusion bodies

The major capsid protein L1 of the human papillomavirus type 16 (HPV16) has been previously expressed recombinantly in Escherichia coli cells as inclusion bodies (IBs). The HPV16 L1 protein offers potential as a vaccine candidate against cervical cancer, but the reported E. coli process is limited in its ability to economically produce significant quantities of material. In this study, a scaleable laboratory process for the purification of recombinant His-tagged L1 protein and its processing to give an immunogenic product is developed. The performances of ion-exchange chromatography (IEX) and immobilised metal affinity chromatography (IMAC) for the purification of L1 protein in the presence of concentrated denaturant are compared. IEX was found to be superior to IMAC when taking into account the complexity of operation, cost of adsorbent, selectivity and purity of the final product. Following purification, reduction of denaturant concentration was performed by dilution to yield a product suitable for formulation. The simplicity and ease of scale-up of dilution makes it an attractive option for process scale production and superior to the existing approach employing dialysis. It was found that direct dilution of denaturant into suitable buffer can give rise to products which have neutralising conformational epitopes identified by strong antibody-binding properties, as assessed by ELISA with a conformational monoclonal antibody. Analysis of the results showed negative main effects of protein concentration and PEG addition on antibody-binding yields, but positive main effects of the addition of detergent and L-arginine to the buffer. The diluted product had antigenic properties as assessed by ELISA and may be formulated easily for use by diafiltration and the addition of adjuvant. This work demonstrates the feasibility of producing viral vaccines using E. coli and scaleable unit operations.     

Purification of enzymatically active human lysyl oxidase and lysyl oxidase-like protein from Escherichia coli inclusion bodies

Lysyl oxidase (LOX) is an extracellular copper dependent enzyme catalyzing lysine-derived cross-links in extracellular matrix proteins. Recent molecular cloning has revealed the existence of a LOX family consisting of LOX and four lysyl oxidase-like proteins (LOXLs; LOXL, LOXL2, LOXL3, and LOXL4). Each member of the LOX family contains a copper-binding domain, residues for lysyl-tyrosyl quinone, and a cytokine receptor-like domain. Very recently, novel functions, such as tumor suppression, cellular senescence, and chemotaxis, have been attributed to this family of amine oxidases, but functional differences among the family members have yet to be determined. For efficient expression and purification, we cloned the cDNAs corresponding to proteolytically processed forms of LOX (LOX-p) and LOXL (LOXL-p1 and LOXL-p2) into a bacterial expression vector pET21a with six continuous histidine codons attached to the 3^′ of the gene. The recombinant proteins were purified with nickel-chelating affinity chromatography and converted into enzymatically active forms by stepwise dialysis in the presence of N-lauroylsarcosinate and Cu²⁺. The purified LOX-p, LOXL-p1, and LOXL-p2 proteins showed specific amine oxidase activity of 0.097, 0.054, and 0.150 U/mg, respectively, which was inhibited by β-aminopropionitrile (BAPN), a specific inhibitor of LOX. Availability of these pure and active forms of LOX and LOXLs will be significantly helpful in functional studies related to substrate specificity and crystal structures of this family of amine oxidases.     

Rapid refolding and polishing of single-chain antibodies from Escherichia coli inclusion bodies

An inexpensive and fast-folding strategy for single-chain antibody (scFv) recovered from Escherichia coli inclusion bodies has been developed. Two anti-fluorescein single-chain antibodies, 4-4-20 and 4M5.3, were expressed as inclusion bodies in E. coli for use in a comparative refolding study. Active protein yields as well as degree of aggregation were evaluated for scFv produced by stepwise dialysis, redox dialysis, and a newly developed controlled dilution and filtration strategy. Although all three methods produced active protein for both 4-4-20 and 4M5.3, the extent of aggregation differed greatly among the methods. For 4-4-20, the controlled dilution and filtration strategy reduced aggregation by half, allowed batch processing times of 8h (an 18-fold improvement), and significantly reduced denaturant usage while increasing active yields by 150%. A hydroxyapatite resin polishing step was used to remove completely the aggregate species and inactive monomeric scFv from active scFv.     

Overexpression of a synthetic gene encoding human alpha interferon in Escherichia coli

Interferons (IFNs) represent an important defense mechanism in vertebrates. In this work, we describe gene synthesis and assembly using the polymerase chain reaction as a method for single-step synthesis of DNA sequences. The oligonucleotides designed were based on Escherichia coli codon usage and two genes of IFN were synthesized: one containing a DNA sequence already known and the other, a mutated form in which two cysteine amino acid residues were replaced by serines in an attempt to improve the stability of the protein. DNA sequences were cloned into pAE, an E. coli vector that allows heterologous protein expression with or without a histidine tag. Recombinant human interferons (rhIFNs) were identified by Western blotting and ELISA using anti-human interferon polyclonal antibodies. Purification of the recombinant His-tagged proteins was achieved in a single step by Ni(2+)-charged column chromatography while proteins without His-tag were purified by extensively washing the inclusion bodies, the final yields being approximately 210 and 75mg/L, respectively. The rhIFNs expressed within this system were biologically active ( approximately 1,1x10(8)IU/mg) based on antiviral assay. The combined methodologies described here proved to be cost-effective and could be extended to other genes/proteins of interest.     

Immunocytochemical demonstration of human proinsulin chimeric polypeptide within cytoplasmic inclusion bodies of Escherichia coli

Immunocytochemical techniques were used to identify human proinsulin chimeric protein in cytoplasmic inclusion bodies of genetically modified Escherichia coli. Antibodies to proinsulin chimeric protein (human proinsulin coupled at its amino-terminus to a portion of the E. coli tryptophan E gene product) were localized in E. coli using post-embedding staining with protein A-peroxidase labelling for transmission electron microscopy. The observable distribution of the labelled antibody was limited to that portion of the E. coli cytoplasm occupied by inclusion bodies. The localization of human peptides as insoluble masses within the bacterial cytoplasm has important implications in relation to the synthesis, recovery and purification of pharmacologically useful substances produced through the application of recombinant DNA technology.     

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.     

Large scale production of biologically active Escherichia coli glutamyl-tRNA reductase from inclusion bodies

Glutamyl-tRNA reductase catalyzes the initial step of tetrapyrrole biosynthesis in plants and prokaryotes. Recombinant Escherichia coli glutamyl-tRNA reductase was purified to apparent homogeneity from an overproducing E. coli strain by a two-step procedure yielding 5.6 mg of enzyme per gram of wet cells with a specific activity of 0.47 micromol min(-1)mg(-1). After recombinant production, denatured glutamyl-tRNA reductase from inclusion bodies was renatured by an on-column refolding procedure. Residual protein aggregates were removed using Superdex 200 gel-filtration chromatography. Solubility, specific activity, and long-term storage properties were improved compared to previous protocols. Obtained enzyme amounts of high purity now allow the research on the recognition mechanism of tRNAGlu and high-throughput inhibitor screening.     

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.