Production of an anti‐Candida peptide via fed batch and ion exchange chromatography

Interest in peptides as diagnostic and therapeutic materials require their manufacture via either a recombinant or synthetic route. This study examined the former, where a recombinant fusion consisting of an antifungal peptide was expressed and isolated from Escherichia coli. Fed batch fermentation with E. coli harboring an arabinose‐inducible plasmid produced the 12 residue anti‐Candida peptide fused to the N‐terminal of Green Fluorescent Protein (GFP_UV). The purification of the fusion protein, using ion‐exchange chromatography, was monitored by using the intrinsic fluorescence of GFP_UV. The recombinant antifungal peptide was successfully released by cyanogen bromide‐induced cleavage of the fusion protein. The recombinant peptide showed the expected antifungal activity. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:865–871, 2016     

Purification of recombinant protein by cold‐coacervation of fusion constructs incorporating resilin‐inspired polypeptides

Polypeptides containing between 4 and 32 repeats of a resilin‐inspired sequence AQTPSSYGAP, derived from the mosquito Anopheles gambiae, have been used as tags on recombinant fusion proteins. These repeating polypeptides were inspired by the repeating structures that are found in resilins and sequence‐related proteins from various insects. Unexpectedly, an aqueous solution of a recombinant resilin protein displays an upper critical solution temperature (cold‐coacervation) when held on ice, leading to a separation into a protein rich phase, typically exceeding 200 mg/mL, and a protein‐poor phase. We show that purification of recombinant proteins by cold‐coacervation can be performed when engineered as a fusion partner to a resilin‐inspired repeat sequence. In this study, we demonstrate the process by the recombinant expression and purification of enhanced Green fluorescent protein (EGFP) in E. coli. This facile purification system can produce high purity, concentrated protein solutions without the need for affinity chromatography or other time‐consuming or expensive purification steps, and that it can be used with other bulk purification steps such as low concentration ammonium sulfate precipitation. Protein purification by cold‐coacervation also minimizes the exposure of the target protein to enhanced proteolysis at higher temperature. Biotechnol. Bioeng. 2012; 109: 2947–2954. © 2012 Wiley Periodicals, Inc.     

Bioproduction and characterization of a pH responsive self‐assembling peptide

Peptide P₁₁‐4 (QQRFEWEFEQQ) was designed to self‐assemble to form β‐sheets and nematic gels in the pH range 5–7 at concentrations ≥12.6 mM in water. This self‐assembly is reversibly controlled by adjusting the pH of the solvent. It can also self‐assemble into gels in biological media. This together with its biocompatibility and biodegradability make P₁₁‐4 an attractive building block for the fabrication of nanoscale materials with uses in, for example, tissue engineering. A limitation to large‐scale production of such peptides is the high cost of solid phase chemical synthesis. We describe expression of peptide P₁₁‐4 in the bacterium Escherichia coli from constructs carrying tandem repeats of the peptide coding sequence. The vector pET31b+ was used to express P₁₁‐4 repeats fused to the ketosteroid isomerase protein which accumulates in easily recoverable inclusion bodies. Importantly, the use of auto‐induction growth medium to enhance cell density and protein expression levels resulted in recovery of 2.5 g fusion protein/L culture in both shake flask and batch fermentation. Whole cell detergent lysis allowed recovery of inclusion bodies largely composed of the fusion protein. Cyanogen bromide cleavage followed by reverse phase HPLC allowed purification of the recombinant peptide with a C‐terminal homoserine lactone (rP₁₁‐4(hsl)). This recombinant peptide formed pH dependent hydrogels, displayed β‐structure measured by circular dichroism and fibril formation observed by transmission electron microscopy. Biotechnol. Bioeng. 2009;103: 241–251. © 2009 Wiley Periodicals, Inc.     

Optimized E. coli expression strain LOBSTR eliminates common contaminants from His‐tag purification

His‐tag affinity purification is one of the most commonly used methods to purify recombinant proteins expressed in E. coli. One drawback of using the His‐tag is the co‐purification of contaminating histidine‐rich E. coli proteins. We engineered a new E. coli expression strain, LOBSTR (lo w b ackground str ain), which eliminates the most abundant contaminants. LOBSTR is derived from the E. coli BL21(DE3) strain and carries genomically modified copies of arnA and slyD, whose protein products exhibit reduced affinities to Ni and Co resins, resulting in a much higher purity of the target protein. The use of LOBSTR enables the pursuit of challenging low‐expressing protein targets by reducing background contamination with no additional purification steps, materials, or costs, and thus pushes the limits of standard His‐tag purifications. Proteins 2013; 81:1857–1861. © 2013 Wiley Periodicals, Inc.     

High‐yield recombinant expression of the chicken antimicrobial peptide fowlicidin‐2 in Escherichia coli

The antimicrobial peptide fowlicidin‐2 identified in chicken is a member of the cathelicidins family. The mature fowlicidin‐2 possesses high antibacterial efficacy and lipopolysaccharide (LPS) neutralizing activity, and also represents an excellent candidate as an antimicrobial agent. In the present study, the recombinant fowlicidin‐2 was successfully produced by Escherichia coli (E. coli) recombinant expression system. The gene encoding fowlicidin‐2 with the codon preference of E. coli was designed through codon optimization and synthesized in vitro. The gene was then ligated into the plasmid pET‐32a(+), which features fusion protein thioredoxin at the N‐terminal. The recombinant plasmid was transformed into E. coli BL21(DE3) and cultured in Luria‐Bertani (LB) medium. After isopropyl‐β‐D‐thiogalactopyranoside (IPTG) induction, the fowlicidin‐2 fusion protein was successfully expressed as inclusion bodies. The inclusion bodies were dissolved and successfully released the peptide in 70% formic acid solution containing cyanogen bromide (CNBr) in a single step. After purification by reverse‐phase high‐performance liquid chromatography (RP‐HPLC), ～6.0 mg of fowlicidin‐2 with purity more than 97% was obtained from 1 litre of bacteria culture. The recombinant peptide exhibited high antibacterial activity against the Gram‐positive and Gram‐negative bacteria, and even drug‐resistant strains. This system could be used to rapidly and efficiently produce milligram quantities of a battery of recombinant antimicrobial peptides as well as for large‐scale production. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:369–374, 2015     

N‐terminal processing of affinity‐tagged recombinant proteins purified by IMAC procedures

The ability of a new class of metal binding tags to facilitate the purification of recombinant proteins, exemplified by the tagged glutathione S‐transferase and human growth hormone, from Escherichia coli fermentation broths and lysates has been further investigated. These histidine‐containing tags exhibit high affinity for borderline metal ions chelated to the immobilised ligand, 1,4,7‐triazacyclononane (tacn). The use of this tag‐tacn immobilised metal ion affinity chromatography (IMAC) system engenders high selectivity with regard to host cell protein removal and permits facile tag removal from the E. coli‐expressed recombinant protein. In particular, these tags were specifically designed to enable their efficient removal by the dipeptidyl aminopeptidase 1 (DAP‐1), thus capturing the advantages of high substrate specificity and rates of cleavage. MALDI‐TOF MS analysis of the cleaved products from the DAP‐1 digestion of the recombinant N‐terminally tagged proteins confirmed the complete removal of the tag within 4‐12 h under mild experimental conditions. Overall, this study demonstrates that the use of tags specifically designed to target tacn‐based IMAC resins offers a comprehensive and flexible approach for the purification of E. coli‐expressed recombinant proteins, where complete removal of the tag is an essential prerequisite for subsequent application of the purified native proteins in studies aimed at delineating the molecular and cellular basis of specific biological processes. Copyright © 2015 John Wiley & Sons, Ltd.     

Pilot-scale production and purification of a staphylokinase-based fusion protein over-expressed in Escherichia coli

SFH, a recombinant staphylokinase-based fusion protein linked by the factor Xa recognition peptide at the N-terminus of hirudin, is a promising therapeutic candidate for thromboembolic diseases. To develop SFH into a new thrombolytic agent, scaled-up production was carried out to provide sufficient preparation for animal safety and clinical studies. Here, we describe a pilot-scale cultivation and purification process for the production of SFH. A high-cell-density fed-batch cultivation for the production of SFH in E. coli was developed in a 40-L bioreactor, which produced about 1.1 g/L of recombinant protein. SFH was purified to homogeneity from the E. coli lysate by expanded bed adsorption chromatography and anion-exchange chromatography, with over 99% purity and 54% recovery. Moreover, the residual endotoxin content was less than 0.5 EU/mL. The molecular weight and in vitro bioactivity of SFH were also determined by electrospray ionization-mass spectrometry (ESI-MS) and fibrinolytic activity assay, respectively.     

Enhanced expression of cysteine‐rich antimicrobial peptide snakin‐1 in Escherichia coli using an aggregation‐prone protein coexpression system

Snakin‐1 (SN‐1) is a cysteine‐rich plant antimicrobial peptide and the first purified member of the snakin family. SN‐1 shows potent activity against a wide range of microorganisms, and thus has great biotechnological potential as an antimicrobial agent. Here, we produced recombinant SN‐1 in Escherichia coli by a previously developed coexpression method using an aggregation‐prone partner protein. Our goal was to increase the productivity of SN‐1 via the enhanced formation of insoluble inclusion bodies in E. coli cells. The yield of SN‐1 by the coexpression method was better than that by direct expression in E. coli cells. After refolding and purification, we obtained several milligrams of functionally active SN‐1, the identity of which was verified by MALDI‐TOF MS and NMR studies. The purified recombinant SN‐1 showed effective antimicrobial activity against test organisms. Our studies indicate that the coexpression method using an aggregation‐prone partner protein can serve as a suitable expression system for the efficient production of functionally active SN‐1. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1520–1528, 2017     

Expression in <Emphasis Type="Italic">Escherichia coli</Emphasis> and purification of bioactive antibacterial peptide ABP-CM4 from the Chinese silk worm, <Emphasis Type="Italic">Bombyx mori</Emphasis>

The antibacterial peptide CM4 (ABP-CM4), isolated from Chinese Bombys mori, is a 35-residue cationic, amphipathic α-helical peptide that exhibits a broad range of antimicrobial activity. To explore a new approach for the expression of ABP-CM4 in E. coli, the gene ABP-CM4, obtained by recursive PCR (rPCR), was cloned into the vector pET32a to construct a fusion expression plasmid. The fusion protein Trx-CM4 was expressed in soluble form, purified by Ni²⁺-chelating chromatography, and cleaved by formic acid to release recombinant CM4. Purification of rCM4 was achieved by affinity chromatography and reverse-phase HPLC. The purified of recombinant peptide showed antimicrobial activities against E. coli K₁₂D₃₁, Penicillium chrysogenum, Aspergillus niger and Gibberella saubinetii. According to the antimicrobial peptide database (http://aps.unmc.edu/AP/main.html), 116 peptides contain a Met residue, but only 5 peptides contain the AspPro site, indicating a broader application of formic acid than CNBr in cleaving fusion protein. The successful application to the expression of the ABP-CM4 indicates that the system is a low-cost, efficient way of producting milligram quantities of ABP-CM4 that is biologically active.     

Production and purification of the phosphoprotein of Nipah virus in <Emphasis Type="Italic">Escherichia coli</Emphasis> for use in diagnostic assays

Nipah Virus (NiV) is an emerging zoonotic paramyxovirus that can be fatal in humans and various types of animals. The phospho (P) protein of NiV plays an important role in RNA synthesis, replication, and genome synthesis. In this study, the NiV P gene was cloned into a pTrcHis2-TOPO vector and the recombinant protein containing a His-tag was produced in Escherichia coli. SDS-PAGE and Western blot analysis using the anti-His antibody confirmed the protein expression. An optimization study of E. coli fermentation showed that the optimal cultivation temperature was 37°C, while the optimal induction time for P protein expression was at 9 h with 1 mM IPTG. Solubility analysis showed that E. coli cultivated at 37°C produced the highest fraction (70%) of soluble P protein. The recombinant P protein was purified from clarified E. coli lysate using an immobilized metal affinity chromatography (IMAC) technique to a purity of 92.67%, with a purification factor of 11.58. The purified P protein strongly reacted with the anti-NiV swine sera collected during a NiV outbreak, suggesting its potential as a diagnostic reagent.     

Expression and purification the antimicrobial peptide CM4 in <Emphasis Type="Italic">Escherichia coli</Emphasis>

The antimicrobial peptide CM4 is a 35-residue cationic peptide. To explore a new approach for the expression and purification of CM4 in Escherichia coli, the CM4 gene was cloned into the vector pET32a to construct an expression vector pET32a-CM4. The fusion protein Trx-CM4, purified by Ni²⁺-chelating chromatography, was cleaved by hydroxylamine hydrochloride to release recombinant CM4. Purification of recombinant CM4 was achieved by reverse HPLC chromatography, and about 1.4 mg/l active recombinant CM4 with the purity more than 98% was obtained. The recombinant CM4 showed antimicrobial activities that were similar to synthetic one. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users. An erratum to this article can be found at     

Production and purification of a cecropin family antibacterial peptide,hinnavin II,in <Emphasis Type="Italic">Escherichia coli</Emphasis>

The antibacterial peptide hinnavin II, isolated from the cabbage butterfly Artogeia rapae, is synthesized with an amidated lysine 37 residue at C-terminus. Glycine-extended native hinnavin II (hinnavin II-38-Gly, hin II) gene with 114 bp coding region was cloned in the expression vector pET-32a (+) to construct a fusion expression plasmid and transformed into Escherichia coli BL21 (DE3) pLysS. The recombinant fusion protein Trx-hin II was expressed in soluble form, purified successfully by Ni²⁺-chelating chromatography, and cleaved by enterokinase to release recombinant hin II (rhin II). Purification of the rhin II was achieved by reversed-phase FPLC, and 2.45 mg pure active rhin II was obtained from 800 mL E. coli culture. The molecular mass of the rhin II determined by MALDI-TOF mass spectrometry is consistent with the theoretical molecular mass of 4,195.0 Da. The purified rhin II showed antimicrobial activities against tested E. coli K 12, E. coli BL21 (DE3), Enterobacter cloacae, Bacillus megaterium, and Staphylococcus aureus. The application of this expression/purification approach represents a fast and efficient method to prepare milligram quantities of hinnavin II in its biologically active form.     

A Targeted LC‐MS Strategy for Low‐Abundant HLA Class‐I‐Presented Peptide Detection Identifies Novel Human Papillomavirus T‐Cell Epitopes

For rational design of therapeutic vaccines, detailed knowledge about target epitopes that are endogenously processed and truly presented on infected or transformed cells is essential. Many potential target epitopes (viral or mutation‐derived), are presented at low abundance. Therefore, direct detection of these peptides remains a challenge. This study presents a method for the isolation and LC‐MS³‐based targeted detection of low‐abundant human leukocyte antigen (HLA) class‐I‐presented peptides from transformed cells. Human papillomavirus (HPV) was used as a model system, as the HPV oncoproteins E6 and E7 are attractive therapeutic vaccination targets and expressed in all transformed cells, but present at low abundance due to viral immune evasion mechanisms. The presented approach included preselection of target antigen‐derived peptides by in silico predictions and in vitro binding assays. The peptide purification process was tailored to minimize contaminants after immunoprecipitation of HLA‐peptide complexes, while keeping high isolation yields of low‐abundant target peptides. The subsequent targeted LC‐MS³ detection allowed for increased sensitivity, which resulted in successful detection of the known HLA‐A2‐restricted epitope E7_11–19 and ten additional E7‐derived peptides on the surface of HPV16‐transformed cells. T‐cell reactivity was shown for all the 11 detected peptides in ELISpot assays, which shows that detection by our approach has high predictive value for immunogenicity. The presented strategy is suitable for validating even low‐abundant candidate epitopes to be true immunotherapy targets.     

Heterologous expression of the <Emphasis Type="Italic">msp2 gene</Emphasis> from <Emphasis Type="Italic">Marasmius scorodonius</Emphasis>

For the heterologous expression of the msp2 gene from the edible mushroom Marasmius scorodonius in Escherichia coli the cDNA encoding the extracellular Msp2 peroxidase was cloned into the pBAD III expression plasmid. Expression of the protein with or without signal peptide was investigated in E. coli strains TOP10 and LMG194. Different PCR products were amplified for expression of the native target protein or a protein with a signal peptide. Omitting the native stop codon and adding six His-residues resulted in a fusion protein amenable to immune detection and purification by immobilised metal affinity chromatography. In E. coli the recombinant protein was produced in high yield as insoluble inclusion bodies. The influence of different parameters on MsP2 refolding was investigated. Active enzyme was obtained by glutathione-mediated oxidation in a medium containing urea, Ca²⁺, and hemin.     

Cloning, Expression, and Purification of the Uropathogenic Escherichia coli Invasin DraD

In this study we presented a very efficient expression system, based on pET30LIC/Ek vector, for producing DraD invasin of the uropathogenic Escherichia coli and a one-step chromatography purification procedure for obtaining pure recombinant protein (DraD-C-His₆). This protein has a molecular weight of 14,818 and calculated pI of 6.6. It contains a polyhistidine tag at the C-terminus (13 additional amino acids) that allowed single-step isolation by Ni affinity chromatography. Also, we obtained specific antibodies against DraD invasin to develop tools for characterizing the expression and biological function of this protein. The amount and quality of DraD-C-His₆ fusion protein purified from E. coli overexpression system seems to be fully appropriate for crystallographic studies (soluble form), and for establishing role of the protein in bacterium (cultured cell line interaction and in the internalization process) and for obtaining rabbit polyclonal antisera (insoluble form).     

A general strategy for the bacterial expression of amyloidogenic peptides using BCL‐XL‐1/2 fusions

Biophysical studies on amyloidogenic and aggregation‐prone peptides often require large quantities of material. However, solid‐phase synthesis, handling, and purification of peptides often present challenges on these scales. Recombinant expression is an attractive alternative because of its low cost, the ability to isotopically label the peptides, and access to sequences exceeding ～50 residues. However, expression systems that seek to solubilize amyloidogenic peptides suffer from low yields, difficult optimizations, and isolation challenges. We present a general strategy for expressing and isolating amyloidogenic peptides in Escherichia coli by fusion to a polypeptide that drives the expression of attached peptides into bacterial inclusion bodies. This scheme minimizes toxicity during bacterial growth and enables the processing and handling of the peptides in denaturing solutions. Immobilized metal affinity chromatography, reverse phase HPLC, and cyanogen bromide cleavage are used to isolate the peptide, followed by further reverse phase HPLC, which yields milligram quantities of the purified peptide. We demonstrate that driving the peptides into inclusion bodies using fusion to BCL‐XL‐1/2 is a general strategy for their expression and isolation, as exemplified by the production of 11 peptides species.     

Bactericidal properties of the antimicrobial peptide Ib-AMP4 from Impatiens balsamina produced as a recombinant fusion-protein in Escherichia coli

Antimicrobial peptides (AMPs) represent a novel class of powerful natural antimicrobial agents. As AMPs are bactericidal, production of AMPs in recombinant bacteria is far from trivial. We report the production of Impatiens balsamina antimicrobial peptide 4 (Ib-AMP4, originally isolated from Impatiens balsamina) in Escherichia coli as a fusion protein and investigate Ib-AMP4's antimicrobial effects on human pathogens. A plasmid vector pET32a-Trx-Ib-AMP4 was constructed and transferred into E. coli. After induction, a soluble fusion protein was expressed successfully. The Ib-AMP4 peptide was obtained with a purity of over 90% after nickel affinity chromatography, ultrafiltration, enterokinase cleavage and sephadex size exclusion chromatography. For maximum activity, Ib-AMP4, which possesses two disulfide bonds, required activation with 5 μg/mL H₂O₂. Antimicrobial assays showed that Ib-AMP4 could efficiently target clinical multiresistant isolates including methicillin-resistant Staphylococcus aureus and extended-spectrum β-lactamase-producing E. coli. Time kill experiments revealed that Ib-AMP4 is bactericidal within 10 min after application. Haemolysis and cytotoxicity assays implied selectivity towards bacteria, an important prerequisite for clinical applications. Ib-AMP4 might be an interesting candidate for clinical studies involving patients with septicemia or for coating clinical devices, such as catheters. The method described here may be applicable for expression and purification of other AMPs with multiple disulfide bridges.     

Purification of His6–organophosphate hydrolase using monolithic supermacroporous polyacrylamide cryogels developed for immobilized metal affinity chromatography

Organophosphate hydrolase containing hexahistidine tag at the N-terminus of recombinant protein (His₆-OPH) and expressed in Escherichia coli cells was purified using supermacroporous polyacrylamide-based monolith columns with immobilized metal affinity matrices [Me²⁺-iminodiacetic acid (IDA)–polyacrylamide cryogel (PAA) and Me²⁺-N,N,N’-tris (carboxymethyl) ethylendiamine (TED)–PAA]. Enzyme preparation with 50% purity was obtained by direct chromatography of nonclarified cell homogenate, whereas the combination of addition of 10 mM imidazole to buffers for cell sonication and sample loading, the use of precolumn with IDA–PAA matrix noncharged with metal ions, and the application of high flow rate provided the 99% purity of enzyme isolated directly from crude cell homogenate. Co²⁺-IDA–PAA provided the highest level of selectivity for His₆-OPH. Comparative analysis of purification using Co²⁺-IDA–PAA and Ni-nitrilotriacetic acid–agarose showed obvious advantages of the former in process time, specific activity of purified enzyme, and simplicity of adsorbent regeneration.     

Cytokine production using membrane adsorbers: Human basic fibroblast growth factor produced by Escherichia coli

Basic fibroblast growth factor (FGF‐2) is a multifunctional cytokine that regulates various cellular processes both in vitro and in vivo. FGF‐2 is extensively used in embryonic stem cell cultures since it can maintain the cells in an undifferentiated state. However, the high price of FGF‐2 has limited its application in stem cell research. Here we present a fast and efficient process for the purification of FGF‐2 from recombinant Escherichia coli cultures using reusable membrane adsorbers. A high expression level of FGF‐2 (42 mg/g dry cell) was achieved by fed‐batch cultivation of E. coli BL21(DE3). A new combination of cation exchange membrane chromatography and heparin‐sepharose affinity chromatography was used for the purification of the protein. A novel anion exchange membrane chromatography was used in the polishing step to remove endotoxins and DNA. In this new process, about 200 mg soluble FGF‐2 was yielded from 1.9 L culture broth with a purity of 98%. The purified protein was identified to be endotoxin‐free and bioactive. It was successfully tested to keep primate embryonic stem cell and human‐induced pluripotent stem cell pluripotent. Our approach, in which a controlled cultivation process is combined with an optimized fast and versatile downstreaming process, is suitable for low‐cost preparation of bioactive FGF‐2 at bench‐scale and may be beneficial to the effective production of other cytokines.     

High‐throughput ion exchange purification of positively charged recombinant protein in the presence of negatively charged dextran sulfate

Product quality analyses are critical for developing cell line and bioprocess producing therapeutic proteins with desired critical product quality attributes. To facilitate these analyses, a high‐throughput small‐scale protein purification (SSP) is required to quickly purify many samples in parallel. Here we develop an SSP using ion exchange resins to purify a positively charged recombinant growth factor P1 in the presence of negatively charged dextran sulfate supplemented to improve the cell culture performance. The major challenge in this work is that the strong ionic interaction between P1 and dextran sulfate disrupts interaction between P1 and chromatography resins. To solve this problem, we develop a two‐step SSP using Q Sepharose Fast Flow (QFF) and SP Sepharose XL (SPXL) resins to purify P1. The overall yield of this two‐step SSP is 78%. Moreover, the SSP does not affect the critical product quality attributes. The SSP was critical for developing the cell line and process producing P1. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:516–520, 2014