Excretion of Human β-Endorphin into Culture Medium by Using Outer Membrane Protein F as a Fusion Partner in Recombinant Escherichia coli

Escherichia coli BL21 strains were found to excrete a large amount of outer membrane protein F (OmpF) into culture medium during high-cell-density cultivation. From this interesting phenomenon, a novel and efficient OmpF fusion system was developed for the excretion of recombinant proteins by E. coli. The ompF gene of E. coli BL21(DE3) was first knocked out by using the red operon of bacteriophage λ to construct E. coli MBEL-BL101. For the excretion of human β-endorphin as a model protein, the β-endorphin gene was fused to the C terminus of the E. coli ompF gene by using a linker containing the Factor Xa recognition site. To develop a fed-batch culture condition that allows efficient production of OmpF-β-endorphin fusion protein, three different feeding strategies, an exponential feeding strategy and two pH-stat strategies with defined and complex nutrient feeding solutions, were examined. Among these, the pH-stat feeding strategy with the complex nutrient feeding solution resulted in the highest productivity (0.33 g of protein per liter per h). Under this condition, up to 5.6 g of OmpF-β-endorphin fusion protein per liter was excreted into culture medium. The fusion protein was purified by anion-exchange chromatography and cleaved by Factor Xa to yield β-endorphin, which was finally purified by reverse-phase chromatography. From 2.7 liters of culture supernatant, 545.4 mg of β-endorphin was obtained.     

Expression,purification, phosphorylation and characterization of recombinant human statherin

This work reports the successful recombinant expression of human statherin in Escherichia coli, its purification and in vitro phosphorylation. Human statherin is a 43-residue peptide, secreted by parotid and submandibular glands and phosphorylated on serine 2 and 3. The codon-optimized statherin gene was synthesized and cloned into commercial pTYB11 plasmid to allow expression of statherin as a fusion protein with intein containing a chitin-binding domain. The plasmid was transformed into E. coli strains and cultured in Luria–Bertani medium, which gave productivity of soluble statherin fusion protein of up to 47 mg per liter of cell culture, while 112 mg of fusion protein were in the form of inclusion bodies. No significant refolded target protein was obtained from inclusion bodies. The amount of r-h-statherin purified by RP–HPLC corresponded to 0.6 mg per liter of cell culture. Attenuated total reflection-Fourier transform infrared spectroscopy experiments performed on human statherin isolated from saliva and r-h-statherin assessed the correct folding of the recombinant peptide. Recombinant statherin was transformed into the diphosphorylated biologically active form by in vitro phosphorylation using the Golgi-enriched fraction of pig parotid gland containing the Golgi-casein kinase.     

High-Level Production of Human Leptin by Fed-Batch Cultivation of Recombinant Escherichia coli and Its Purification

Human leptin is a 16-kDa (146-amino-acid) protein that is secreted from adipocytes and influences body weight homeostasis. In order to obtain high-level production of leptin, the human obese gene coding for leptin was expressed in Escherichia coli BL21(DE3) under the strong inducible T7 promoter. The recombinant leptin was produced as inclusion bodies in E. coli, and the recombinant leptin content was as high as 54% of the total protein content. For production of recombinant human leptin in large amounts, pH-stat fed-batch cultures were grown. Expression of leptin was induced at three different cell optical densities at 600 nm (OD₆₀₀), 30, 90, and 140. When cells were induced at an OD₆₀₀ of 90, the amount of leptin produced was 9.7 g/liter (37% of the total protein). After simple purification steps consisting of inclusion body isolation, denaturation and refolding, and anion-exchange chromatography, 144.9 mg of leptin that was more than 90% pure was obtained from a 50-ml culture, and the recovery yield was 41.1%.     

Production of recombinant Chikungunya virus envelope 2 protein in Escherichia coli

Chikungunya, a mosquito-borne viral disease caused by Chikungunya virus (CHIKV), has drawn substantial attention after its reemergence causing massive outbreaks in tropical regions of Asia and Africa. The recombinant envelope 2 (rE2) protein of CHIKV is a potential diagnostic as well as vaccine candidate. Development of cost-effective cultivation media and appropriate culture conditions are generally favorable for large-scale production of recombinant proteins in Escherichia coli. The effects of medium composition and cultivation conditions on the production of recombinant Chikungunya virus E2 (rCHIKV E2) protein were investigated in shake flask culture as well as batch cultivation of Escherichia coli. Further, the fed-batch process was also carried out for high cell density cultivation of E. coli expressing rE2 protein. Expression of rCHIKV E2 protein in E. coli was induced with 1 mM isopropyl-beta-thiogalactoside (IPTG) at ~23 g dry cell weight (DCW) per liter of culture and yielded an insoluble protein aggregating to form inclusion bodies. The final DCW after fed-batch cultivation was ~35 g/l. The inclusion bodies were isolated, solubilized in 8 M urea and purified through affinity chromatography to give a final product yield of ~190 mg/l. The reactivity of purified E2 protein was confirmed by Western blotting and enzyme-linked immunosorbent assay. These results show that rE2 protein of CHIKV may be used as a diagnostic reagent or for further prophylactic studies. This approach of producing rE2 protein in E. coli with high yield may also offer a promising method for production of other viral recombinant proteins.     

A Mutation That Improves Soluble Recombinant Hemoglobin Accumulation in Escherichia coli in Heme Excess

High-level expression of soluble recombinant human hemoglobin (rHb) in Escherichia coli was obtained with several hemoglobin variants. Under identical conditions, two rHbs containing the Presbyterian mutation (Asn-108→Lys) in β-globin accumulated to approximately twofold less soluble globin than rHbs containing the corresponding wild-type β-globin subunit accumulated. The β-globin Providence_(asp) mutation (Lys-82→Asp) significantly improved soluble rHb accumulation compared to the wild-type β-globin subunit and restored soluble accumulation of rHbs containing the Presbyterian mutation to wild-type levels. The Providence_asp substitution introduced a negatively charged residue into the normally cationic 2,3-bisphosphoglycerate binding pocket, potentially reducing the electrostatic repulsion in the absence of the polyanion. The average soluble globin accumulation when there was coexpression of di-α-globin and β-Lys-82→Asp-globin (rHb9.1) and heme was present in at least a threefold molar excess was 36% ± 3% of the soluble cell protein in E. coli. The average total accumulation (soluble globin plus insoluble globin) was 56% ± 7% of the soluble cell protein. Fermentations yielded 6.0 ± 0.3 g of soluble rHb9.1 per liter 16 h after induction and 6.4 ± 0.2 g/liter 24 h after induction. The average total globin yield was 9.4 g/liter 16 h after induction. High-level accumulation of soluble rHb in E. coli depends on culture conditions, the protein sequence, and the molar ratio of the heme cofactor added.     

Overexpression in E. coli and Purification of the L. pneumophila Lpp2981 Protein

The Lpp2981 gene from Legionella pneumophila, the causative agent of Legionnaire’s disease, was cloned into the pMWT7 plasmid. The construct was used to express this gene in Escherichia coli. Five different bacterial strains were tested to overexpress the gene but without success. Sequence analysis revealed a cluster of four rare codons near the 5′-end of the gene. These codons were replaced with those commonly used in E. coli. The mutated Lpp2981 gene was successfully expressed in all the E. coli strains tested. The expressed protein (with an apparent molecular mass of 30 kDa) was collected in the insoluble fraction of the cell lysate, purified as inclusion bodies and functionally reconstituted into liposomes. The highest level of overexpression was obtained in E. coli C0214 after 6 h of induction with isopropyl-β-d-thiogalactopyranoside at 37 °C, yielding 74 mg of purified protein per liter of culture. We conclude that the clustering of rare codons at the 5′-end of the open-reading frame is a critical factor for the heterologous expression of Lpp2981 in E. coli.     

High-yield expression and purification of soluble forms of the anti-apoptotic Bcl-x(L) and Bcl-2 as TolAIII-fusion proteins

A method is presented to produce large amounts of Bcl-2 and Bcl-x_L, two anti-apoptotic proteins of considerable biomedical interest. Expression constructs were prepared in which the Escherichia coli protein TolAIII, known to promote over expression of soluble product, was added to the N-terminus of Bcl-2 or Bcl-x_L proteins, which had their C-terminal hydrophobic anchors deleted. Here the expression of these TolAIII-fusion constructs, followed by a two-step metal-affinity based purification protocol is described. The method delivers at least 20 and 10 mg of more than 90% pure TolAIII-Bcl-x_LΔC and TolAIII-Bcl-2(2)ΔC proteins, respectively, per liter of E. coli cell culture. The proteins are released by proteolysis with thrombin providing >12 mg of Bcl-x_LΔC or >6 mg of Bcl-2(2)ΔC per liter of E. coli cell culture with a purity of more than 95%. Whereas Bcl-x_LΔC is soluble both before and after TolAIII removal, Triton X-100 can significantly increase the extraction of TolAIII- Bcl-2(2)ΔC from the bacterial cells and its subsequent solubility. Far-UV CD spectroscopy demonstrated that they both have an α-helical structure. Fluorescence spectroscopy was used to quantitatively analyze the binding of the respiratory inhibitor antimycin A to recombinant Bcl-2 and Bcl-x_L proteins as well as the displacement of this ligand from the hydrophobic pocket with BH3 Bad-derived peptide. Purified Bcl-x_LΔC and Bcl-2(2)ΔC both protect isolated mitochondria from Bax-induced release of cytochrome c. The ensemble of data shows that the expressed proteins are correctly folded and functional. Therefore, the TolAIII-fusion system provides a convenient tool for functional characterization and structural studies of anti-apoptotic proteins.     

Factors Affecting Oxidation of Thiosalts by Thiobacilli

The effects of temperature, initial pH, and the concentrations of ammonium, phosphate, and heavy metals on the oxidation of thiosalts by an authentic strain of Thiobacillus thiooxidans (ATCC 8085) and by a mixed culture isolated from a base metal-processing mill effluent pond were studied. The optimum temperature was 30°C and the optimum initial pH was 3.75 for both cultures using thiosulfate and for the mixed culture using tetrathionate. T. thiooxidans ATCC 8085 did not oxidize tetrathionate. For a thiosalt concentration of 2,000 ppm (2,000 mg/liter), maximal rates of destruction occurred at concentrations of ammonium ion above 2 mg/liter and in the presence of 1 mg of phosphate per liter. Under optimal conditions, the rate of thiosulfate oxidation by the pure culture was 55 ± 3 mg/liter per h; the mixed culture oxidized thiosulfate at the rate of 40 ± 1 mg/liter per h and tetrathionate at the rate of 50 ± 2 mg/liter per h. Metal ions caused normal inhibition kinetics in the oxidation of thiosulfate by T. thiooxidans ATCC 8085. K_i values were calculated for cadmium (16 mg/liter), copper (0.46 mg/liter), lead (2 mg/liter), silver (3.1 mg/liter), and zinc (33 mg/liter). Only a slight additive effect was apparent in the presence of all of these metal ions. The mixed culture of thiosalt-oxidizing bacteria was less sensitive to heavy metal inhibition; the order of inhibition of thiosulfate oxidation was Cd < Zn < Pb < Ag < Cu, and that of tetrathionate oxidation was Zn < Cd < Pb < Ag < Cu.     

Isoprene Production Via the Mevalonic Acid Pathway in Escherichia coli (Bacteria)

There is a need to develop renewable fuels and chemicals that will help meet global demands for energy and synthetic chemistry feedstock, without contributing to climate change or environmental degradation. Isoprene (C₅H₈) is one such key chemical ingredient, required for the production of synthetic rubber or plastic products, and a potential biofuel. Enabling a sustainable microbial fermentation for the production of isoprene is an attractive alternative to a petroleum origin. This work demonstrates transgenic expression of the Pueraria montana (kudzu vine) isoprene synthase gene (kIspS) and heterologous isoprene production in Escherichia coli. Enhancements in the amount of E. coli isoprene production were achieved upon over-expression of the native 2-C-methyl-d-erythritol-4-phosphate (MEP) biosynthetic pathway and, independently, upon heterologous over-expression of the entire mevalonic acid (MVA) pathway. A direct comparison of the efficiency of cellular organic carbon flux through the MEP and MVA pathways is provided, under conditions when these are expressed in the same host using the same plasmid, and same ribosome-binding sites (RBS). These alternative isoprenoid biosynthetic pathways were assembled in and expressed through a superoperon, suitable for transformation of E. coli. Introduction of specific RBS and nucleotide spacers between individual genes in the superoperon structure enabled maximal expression in E. coli batch cultures and translated to an improved production from 0.4?mg isoprene per liter of culture (control) to 5?mg isoprene per liter of culture (MEP superoperon transformants) and up to 320?mg isoprene per liter of culture (MVA superoperon transformants). This 800-fold increase in isoprene concentration from the MVA transformants and the attendant isoprene-to-biomass 0.78:1 carbon partitioning ratio suggested that the engineered MVA pathway introduces a bypass in the flux of endogenous substrate in E. coli to isopentenyl-diphosphate and dimethylallyl-diphosphate, thus overcoming flux limitations imposed upon the regulation of the native MEP pathway by the cell.     

Process and Metabolic Strategies for Improved Production of Escherichia coli-Derived 6-Deoxyerythronolide B

Recently, the feasibility of using Escherichia coli for the heterologous biosynthesis of complex polyketides has been demonstrated. In this report, the development of a robust high-cell-density fed-batch procedure for the efficient production of complex polyketides is described. The effects of various physiological conditions on the productivity and titers of 6-deoxyerythronolide B (6dEB; the macrocyclic core of the antibiotic erythromycin) in recombinant cultures of E. coli were studied in shake flask cultures. The resulting data were used as a foundation to develop a high-cell-density fermentation procedure by building upon procedures reported earlier for recombinant protein production in E. coli. The fermentation strategy employed consistently produced ~100 mg of 6dEB per liter, whereas shake flask conditions generated between 1 and 10 mg per liter. The utility of an accessory thioesterase (TEII from Saccharopolyspora erythraea) for enhancing the productivity of 6dEB in E. coli was also demonstrated (increasing the final titer of 6dEB to 180 mg per liter). In addition to reinforcing the potential for using E. coli as a heterologous host for wild-type- and engineered-polyketide biosynthesis, the procedures described in this study may be useful for the production of secondary metabolites that are difficult to access by other routes.     

Efficient Expression and Rapid Purification of Human T-Cell Leukemia Virus Type 1 Protease

Human T-cell leukemia virus type 1 (HTLV-1) is an oncovirus that is clinically associated with adult T-cell leukemia. We report here the construction of a pET19-based expression clone containing HTLV-1 protease fused to a decahistidine-containing leader peptide. The recombinant protein is efficiently expressed in Escherichia coli, and the fusion protein can be easily purified by affinity chromatography. Active mature protease in yields in excess of 3 mg/liter of culture can then be obtained by a novel two-step refolding and autoprocessing procedure. The purified enzyme exhibited K_m and K_cat values of 0.3 mM and 0.143 sec⁻¹ at pH 5.3 and was inhibited by pepstatin A.     

Production of bioactive human hemangiopoietin in <Emphasis Type="Italic">Escherichia coli</Emphasis>

To devise an efficient approach for production of human hemangiopoietin (hHAPO), the gene of hHAPO was synthesized and subcloned into the pSUMO vector with a SUMO tag at the N-terminus. The expression construct was then transformed into the expression strain E. coli BL21(DE3). The fusion protein was expressed in soluble form and identified by SDS-PAGE and Western blotting. The fusion protein was purified to 90% purity by metal chelate chromatography with a yield of 45 mg per liter fermentation culture. The SUMO tag was removed by cleavage with SUMO protease at room temperature for 1 h, and the hHAPO was then re-purified by the metal chelate chromatography. Finally, about 21 mg hHAPO was obtained from 1 liter of fermentation culture with no less than 95% purity. The recombinant hHAPO significantly stimulated the proliferation of human umbilical vein endothelial cells.     

The Small Metal-Binding Protein SmbP Improves the Expression and Purification of the Recombinant Antitumor-Analgesic Peptide from the Chinese Scorpion Buthus martensii Karsch in Escherichia coli

We have recently shown that SmbP, the small metal-binding protein of Nitrosomonas europaea, can be employed as a fusion protein to express and purify recombinant proteins and peptides in Escherichia coli. SmbP increases solubility, allows simple, one-step purification through affinity chromatography, and provides superior final yields due to its low molecular weight. In this work, we report for the first time the use of SmbP to produce a recombinant peptide with anticancer activity: the antitumor-analgesic peptide (BmK-AGAP), a neurotoxin isolated from the venom of the Chinese scorpion Buthus martensii Karsch. This peptide was expressed in Escherichia coli SHuffle for correct, cytoplasmic, disulfide bond formation and tagged with SmbP at the N-terminus to improve its solubility and allow purification using immobilized metal affinity chromatography. SmbP_BmK-AGAP was found in the soluble fraction of the cell lysate. After purification and removal of SmbP by digestion with enterokinase, 1.8 mg of pure and highly active rBmK-AGAP was obtained per liter of cell culture. rBmK-AGAP exhibited antiproliferative activity on the MCF-7 cancer cell line, with a half-maximal inhibitory concentration value of 7.24 μM. Based on these results, we considered SmbP to be a suitable carrier protein for the production of recombinant, biologically active BmK-AGAP. We propose that SmbP should be an attractive fusion protein for the expression and purification of additional recombinant proteins or peptides that display anticancer activities.     

Microbial Conversion of Acetanilide to 2′-Hydroxyacetanilide and 4′-Hydroxyacetanilide

Approximately 700 cultures of various types were examined for their ability to hydroxylate acetanilide. The major product formed by unidentified Streptomyces species RJTS-539 was identified as 4′-hydroxyacetanilide (N-acetyl-p-aminophenol). This culture gave a peak yield of 405 mg per liter from 1,000 mg of acetanilide per liter. Considerably lower yields of 4′-hydroxyacetanilide were isolated from S. cinnamoneus NRRLB-1285. The major conversion product of acetanilide formed by Amanita muscaria F-6 was identified as 2′-hydroxyacetanilide, with a peak yield of 433 mg per liter from 1,000 mg per liter of substrate. A small amount of 4′-hydroxyacetanilide was also formed. Six other Streptomyces cultures formed small amounts of one or two products identical or similar to 2′-hydroxyacetanilide or 4′-hydroxyacetanilide as determined by thin-layer chromatography and ultraviolet spectra.     

Microbial conversion of acetanilide to 2'-hydroxyacetanilide and 4'-hydroxyacetanilide

Approximately 700 cultures of various types were examined for their ability to hydroxylate acetanilide. The major product formed by unidentified Streptomyces species RJTS-539 was identified as 4′-hydroxyacetanilide (N-acetyl-p-aminophenol). This culture gave a peak yield of 405 mg per liter from 1,000 mg of acetanilide per liter. Considerably lower yields of 4′-hydroxyacetanilide were isolated from S. cinnamoneus NRRLB-1285. The major conversion product of acetanilide formed by Amanita muscaria F-6 was identified as 2′-hydroxyacetanilide, with a peak yield of 433 mg per liter from 1,000 mg per liter of substrate. A small amount of 4′-hydroxyacetanilide was also formed. Six other Streptomyces cultures formed small amounts of one or two products identical or similar to 2′-hydroxyacetanilide or 4′-hydroxyacetanilide as determined by thin-layer chromatography and ultraviolet spectra.     

Construction of a Low-Temperature Protein Expression System Using a Cold-Adapted Bacterium, Shewanella sp. Strain Ac10, as the Host

A recombinant protein expression system working at low temperatures is expected to be useful for the production of thermolabile proteins. We constructed a low-temperature expression system using an Antarctic cold-adapted bacterium, Shewanella sp. strain Ac10, as the host. We evaluated the promoters for proteins abundantly produced at 4°C in this bacterium to express foreign proteins. We used 27 promoters and a broad-host-range vector, pJRD215, to produce β-lactamase in Shewanella sp. strain Ac10. The maximum yield was obtained when the promoter for putative alkyl hydroperoxide reductase (AhpC) was used and the recombinant cells were grown to late stationary phase. The yield was 91 mg/liter of culture at 4°C and 139 mg/liter of culture at 18°C. We used this system to produce putative peptidases, PepF, LAP, and PepQ, and a putative glucosidase, BglA, from a psychrophilic bacterium, Desulfotalea psychrophila DSM12343. We obtained 48, 7.1, 28, and 5.4 mg/liter of culture of these proteins, respectively, in a soluble fraction. The amounts of PepF and PepQ produced by this system were greater than those produced by the Escherichia coli T7 promoter system.     

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.     

Production of Resveratrol in Recombinant Microorganisms

Resveratrol production in Saccharomyces cerevisiae was compared to that in Escherichia coli. In both systems, 4-coumarate:coenzyme A ligase from tobacco and stilbene synthase from grapes were expressed. When p-coumaric acid was used as the precursor, resveratrol accumulations in the culture medium were observed to be comparable in E. coli (16 mg/liter) and yeast (6 mg/liter).     

Over-Expression in <Emphasis Type="Italic">E. coli</Emphasis> and Purification of the Human OCTN2 Transport Protein

The OCTN2 cDNA amplified from human skin fibroblast was cloned in pET-41a(+) carrying the glutathione S-transferase (GST) gene. The construct pET-41a(+)–hOCTN2 was used to express the GST–hOCTN2 fusion protein in Escherichia coli Rosetta(DE3)pLysS. The best over-expression was obtained after 6 h of induction with IPTG at 28°C. The GST–hOCTN2 polypeptide was collected in the inclusion bodies and showed an apparent molecular mass on SDS-PAGE of 85 kDa. After solubilization with a buffer containing 0.8% sarkosyl and 3 M urea, the fusion protein was applied onto a Ni²⁺-chelating chromatography column. The purified GST–hOCTN2 was treated with thrombin, and the hOCTN2 was separated from the GST by size exclusion chromatography. After the whole procedure, a yield of about 0.2 mg purified protein per liter of cell culture was obtained. To improve the protein yield, hOCTN2 cDNA was subjected to codon bias. The second codon CGG was substituted with AAA; the substitution led to the mutation R2K in the hOCTN2 protein. hOCTN2(R2K) cDNA was cloned in pET-21a(+) carrying a C-terminal 6His tag. The resulting protein was expressed in E. coli Rosetta(DE3)pLysS and purified by Ni²⁺-chelating chromatography. A yield of about 3.5 mg purified protein per liter of cell culture was obtained with this procedure.     

Heterologous expression and isolation of influenza A virus nuclear export protein NEP

Influenza A virus nuclear export protein NEP (NS2, 14.4 kDa) plays a key role in various steps of the virus life cycle. Highly purified protein preparations are required for structural and functional studies. In this study, we designed a series of Escherichia coli plasmid constructs for highly efficient expression of the NEP gene under control of the constitutive trp promoter. An efficient method for extraction of NEP from inclusion bodies based on dodecyl sulfate treatment was developed. Preparations of purified NEP with either N-or C-terminal (His)₆-tag were obtained using Ni-NTA agarose affinity chromatography with yield of more than 20 mg per liter of culture. According to CD data, the secondary structure of the proteins matched that of natural NEP. A high propensity of NEP to aggregate over a wide range of conditions was observed.