The purification of TEM-β-lactamase from cell extract using immobilized copper affinity chromatography

Summary TEM--lactamase was purified by immobilized metal affinity chromatography from E. coli cell extracts. It was hypothesized that this protein could be purified in one step due to the abundence of metal binding residues. A pH gradient eluted the cell extract proteins. EDTA treatment released TEM--lactamase. This procedure is much simpler than the current methods employed for TEM--lactamase purification.     

Chaperone over-expression in Escherichia coli: Apparent increased yields of soluble recombinant protein kinases are due mainly to soluble aggregates

The recombinant expression of eukaryotic proteins in Escherichia coli often results in protein aggregation. Several articles report on improved solubility and increased purification yields of individual proteins upon over-expression of E. coli chaperones but this effect might potentially be protein-specific. To find out whether chaperone over-expression is a generally applicable strategy for the production of human protein kinases in E. coli, we analyzed 10 kinases, mainly as catalytic domain constructs. The kinases studied, namely c-Src, c-Abl, Hck, Lck, Igf1R, InsR, KDR, c-Met, b-Raf and Irak4, belong to the tyrosine and tyrosine kinase-like groups of kinases. Upon over-expression of the E. coli chaperones DnaK/DnaJ/GrpE and GroEL/GroES, the yields of 7 from 10 polyhistidine-tagged kinases were increased up to 5-fold after nickel-affinity purification (IMAC). Additive over-expression of the chaperones ClpB and/or trigger factor showed no further improvement. Co-purification of DnaJ and GroEL indicated incomplete kinase folding, therefore, the oligomerization state of the kinases was determined by size-exclusion chromatography. In our study, kinases behave in three different ways. Kinases where yields are not affected by E. coli chaperone over-expression e.g. c-Src elute in the monomeric fraction (category I). Although IMAC yields increase upon chaperone over-expression, InsR and b-Raf kinase are present as soluble aggregates (category II). Igf1R and c-Met kinase catalytic domains are partially complexed with E. coli chaperones upon over-expression; however, they show 2-fold increased yields of monomer (category III). Together, our results suggest that the benefits of chaperone over-expression on the production of protein kinases in E. coli are indeed case-specific.     

Efficient and easily scalable protein folding strong anion exchange chromatography for renaturation and simultaneous purification of recombinant human asparaginase from E. coli

Recombinant proteins are revolutionizing present day therapeutics. They are generally expressed as insoluble inclusion bodies in the E. coli and mis‐folding, loss of protein, and high cost of down streaming are the hurdles in their recovery. For the first time, we are reporting the refolding with simultaneous purification of rhASP in E. coli using a single step utilizing protein folding‐strong anion exchange chromatography (PF‐SAX). The purification method is also standardized for optimal concentration of solution additives, pH, and mobile phase composition. The results showed purification of rhASP with anion exchange chromatography was effective. Phosphate buffer and slightly alkaline pH produced significant recovery yields and purity profiles. The effect of solution additives such as arginine, glycerol, TMAO, sorbitol, dextran, glutamate, and fructose on rhASP renaturation is also investigated. Significant results were achieved using arginine‐TMAO combination in terms of purity, recovery yield and specific activity of 99%, 78%, and 210 IU/mg, respectively. The work concludes that PF‐SAX refolding method is superior to other conventional methods and it can be applied to large scale purification of rhASP produced in E. coli. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:1036–1044, 2018     

Restriction enzyme cleavage of DNA resulting from gently lysed Escherichia coli.

Summary When E. coli or infected E. coli are gently lysed the DNA is released as a very fast sedimenting species that is presumably bound to membrane material. If this complex is now subjected to restriction enzyme cleavage, only a minor fraction of the fast sedimenting DNA remains and this is found, after purification, to be enriched for branched molecules.     

Bacterial production of latarcin 2a, a potent antimicrobial peptide from spider venom

Natural venoms are promising sources of candidate therapeutics including antibiotics. A recently described potent antimicrobial peptide latarcin 2a (Ltc 2a) from Lachesana tarabaevi spider venom shows a broad-spectrum antibacterial activity. This peptide consists of 26 amino acid residues and therefore its production using chemical synthesis, although trivial, is costly. We describe an easy approach to Ltc 2a production in Escherichia coli using the conventional fusion partner thioredoxin. Latarcin 2a synthetic gene was cloned into the expression vector pET-32b, which was then used to transform E. coli BL21(DE3) strain. His-tagged fusion purification was achieved using metal-chelate affinity chromatography. Since no methionine residues are present in the latarcin 2a sequence, cyanogen bromide could be effectively utilized to separate the target product from the carrier protein. Reverse-phase HPLC was used as the final step of purification; the final yield was 3 mg/L of bacterial culture. To increase the yields, we attempted incorporation of Ltc 2a tandem repeats into the fusion protein; however, production rates greatly decreased due to enhanced fusion toxicity. Moreover, we probed constructs to produce an Ltc 2a dimer and the Ltc 2a propeptide to study their functional properties. Recombinant peptides were produced at appreciable yields and biological tests to determine their activities were performed. Latarcin 2a is the first linear peptide from spider venom and one of the first membrane-active peptides from venomous animals to be biosynthetically produced.     

Purification of fusion proteins using affinity microspheres in aqueous two-phase systems

Affinity microspheres were prepared by immobilizing human -globulin (HGb) onto carboxylated poly (styrene/acrylamide) latex particles [P(St/AAm)-H; average diameter 0.33 m], which were prepared by emulsifier-free emulsion polymerization. HGB was covalently immobilized onto the latex particles with high efficiency by the carbodiimide method. A fusion protein (ZZB1B2) of immunoglobulin G and albumin-binding domains (ZZ and B1B2, respectively) was expressed intracellularly and extracellularly in Escherichia coli and was purified by the affinity microspheres. In poly (ethylene glycol) (PEG)/potassium phosphate aqueous two-phase system, the affinity microspheres were partitioned into the PEG-rich top phase, while cells and cell debris of E. coli were displaced into the salt-rich bottom phase. Therefore, ZZB1B2 was directly purified from cell disintegrate or culture broth by combining the affinity microspheres with the aqueous two-phase partitioning, and its purity was almost the same as that purified by conventional affinity chromatography. Therefore, by this purification method, the primary purification process and the subsequent high resolution purification process are combined, and the number of purification steps can be reduced. Correspondence to: A. Kondo     

NADH oxidase ofThermus thermophilus HB8 overproduced fromEscherichia coli

Summary An NADH oxidase purified from the extreme thermophileThermus thermophilus HB8 is a monomeric flavoprotein with a 1 1 ratio of flavin-adenine dinucleotide (FAD) to the polypeptide chain. It catalyzes in vitro the oxidation of reduced NADH or NADPH with the formation of H₂O₂. The gene encoding the NADH oxidase fromT. thermophilus HB8 was cloned, and its nucleotide sequence was determined. The molecular mass of 22,749 Da, as deduced from thenox gene, agrees with that of the purified NADH oxidase fromT. thermophilus HB8, as estimated by mass spectrometry. Thenox gene does not contain a GX₄GK consensus sequence typical for nucleotide binding proteins. Thenox gene was overexpressed inEscherichia coli, and a protocol for the rapid purification of theE. coli-borneT. thermophilus NADH oxidase or its His₆-tagged analogue was developed by using thermal denaturation step and affinity chromatography.     

Cloning of proline-specific endopeptidase gene from Flavobacterium meningosepticum: expression in Escherichia coli and purification of the heterologous protein

Proline-specific endopeptidase (PSE) (EC 3.4.21.26) from Flavobacterium meningosepticum was subjected to partial amino acid sequencing. According to the peptide sequences obtained, oligonucleotides were used to amplify a PSE-specific DNA fragment of 930 bp from F. meningosepticum genomic DNA, employing the polymerase chain reaction technique. This fragment served as a molecular probe to isolate the respective gene. DNA sequencing revealed that the PSE gene consists of 2118 bp coding for a 78,634 Da protein of 705 amino acids. The coding region was cloned in different expression vectors of Escherichia coli. Transformed E. coli cells overproduce an active prolyl endopeptidase of 75,000 relative molecular mass, which is delivered to the bacterial periplasmic space. Up to 1.6 units of active prolyl endopeptidase were obtained from 1 mg E. coli cells. Furthermore, the efficient purification of active prolyl endopeptidase from the periplasm of recombinant E. coli cells is described. Correspondence to: G. Reipen     

The fermentation process for l-phenylalanine production using an auxotrophic regulatory mutant of Escherichia coli

Summary A process for l-phenylalanine production was studied using a tyrosine auxotrophic regulatory mutant of Escherichia coli, resistant to both -2-thienyl-dl-alanine and p-fluoro-dl-phenylalanine. Fermentations were carried out in a 30-1 fermentor with intermittent feeding of glucose plus phosphate. The mutant accumulated l-phenylalanine in the fermentation broth up to 15 g/l at pH 7.0 and 33°C. Column chromatography on a strong cation exchanger was employed as the most effective step in the purification of l-phenyl-alanine from the broth. This step brought about 4-fold concentration of the product with 96% recovery.     

Isolation and functional identification of a novel cDNA for astaxanthin biosynthesis from Haematococcus pluvialis,and astaxanthin synthesis in Escherichia coli

We succeeded in isolating a novel cDNA involved in astaxanthin biosynthesis from the green alga Haematococcus pluvialis, by an expression cloning method using an Escherichia coli transformant as a host that synthesizes -carotene due to the Erwinia uredovora carotenoid biosynthesis genes. The cloned cDNA was shown to encode a novel enzyme, -carotene ketolase (-carotene oxygenase), which converted -carotene to canthaxanthin via echinenone, through chromatographic and spectroscopic analysis of the pigments accumulated in an E. coli transformant. This indicates that the encoded enzyme is responsible for the direct conversion of methylene to keto groups, a mechanism that usually requires two different enzymatic reactions proceeding via a hydroxy intermediate. Northern blot analysis showed that the mRNA was synthesized only in the cyst cells of H. pluvialis. E. coli carrying the H. pluvialis cDNA and the E. uredovora genes required for zeaxanthin biosynthesis was also found to synthesize astaxanthin (3S, 3S), which was identified after purification by a variety of spectroscopic methods.     

Engineering the lac permease for purification and crystallization

The lactose permease is being used as a model system for the rational redesign of a membrane protein with the goal of increasing the likelihood of crystallization. Various modifications to the protein have been added for the purposes of purification, stability, and potential for crystallization. The addition of six consecutive histidines at the C-terminus of the protein allows for the rapid purification by nickel-chelate chromatography, and the insertion of an entire protein domain into one of the inner cytoplasmic loops of the permease gives the resulting protein a larger hydrophilic surface area. The increase in polar surface area makes the fusion protein easier to handle and more likely to crystallize. In particular, the introduction of cytochromeb562 ofE. coli into the central hydrophilic domain of the lac permease results in a fusion protein with the transport activity of the permease and the visible absorbance spectrum of the cytochrome. The red permease is very easy to monitor through the steps of expression, purification, concentration, and crystallization.     

Isotopically labeled expression in E. coli, purification, and refolding of the full ectodomain of the influenza virus membrane fusion protein

This paper describes methods to produce an isotopically labeled 23 kDa viral membrane protein with purified yield of 20 mg/L of Escherichia coli shake flask culture. This yield is sufficient for NMR structural studies and the protein production methods are simple, straightforward, and rapid and likely applicable to other recombinant membrane proteins expressed in E. coli. The target FHA2 protein is the full ectodomain construct of the influenza virus hemagglutinin protein which catalyzes fusion between the viral and the cellular endosomal membranes during infection. The high yield of FHA2 was achieved by: (1) initial growth in rich medium to A₆₀₀  8 followed by a switch to minimal medium and induction of protein expression; and (2) obtaining protein both from purification of the detergent-soluble lysate and from solubilization, purification, and refolding of inclusion bodies. The high cell density was achieved after optimization of pH, oxygenation, and carbon source and concentration, and the refolding protocol was optimized using circular dichroism spectroscopy. For a single residue of membrane-associated FHA2 that was obtained from purification and refolding of inclusion bodies, native conformation was verified by the ¹³CO chemical shifts measured using solid-state nuclear magnetic resonance spectroscopy.     

High-yield expression and purification of a monotopic membrane glycosyltransferase

Membrane proteins are essential to many cellular processes. However, the systematic study of membrane protein structure has been hindered by the difficulty in obtaining large quantities of these proteins. Protein overexpression using Escherichia coli is commonly used to produce large quantities of protein, but usually yields very little membrane protein. Furthermore, optimization of the expressing conditions, as well as the choice of detergent and other buffer components, is thought to be crucial for increasing the yield of stable and homogeneous protein. Herein we report high-yield expression and purification of a membrane-associated monotopic protein, the glycosyltransferase monoglucosyldiacylglycerol synthase (alMGS), in E. coli. Systematic optimization of protein expression was achieved through controlling a few basic expression parameters, including temperature and growth media, and the purifications were monitored using a fast and efficient size-exclusion chromatography (SEC) screening method. The latter method was shown to be a powerful tool for fast screening and for finding the optimal protein-stabilizing conditions. For alMGS it was found that the concentration of detergent was just as important as the type of detergent, and a low concentration of n-dodecyl-β-d-maltoside (DDM) (1× critical micelle concentration) was the best for keeping the protein stable and homogeneous. By using these simply methods to optimize the conditions for alMGS expression and purification, the final expression level increase by two orders of magnitude, reaching 170 mg of pure protein per litre culture.     

New recombinant producer of human ω-amidase based on <Emphasis Type="Italic">Escherichia coli</Emphasis>

A new artificial gene encoding human ω-amidase (Nit2) adapted for highly efficient expression in E. coli has been established. A pQE-Nit2 plasmid construct controlled by the T5 promoter has been engineered for its expression. The nit2 gene within the pQE-Nit2 construct has optimized codon usage and an artificial 6His-tag sequence inserted directly after the ATG initiation codon. This tag provides the possibility of single-step purification of a product via metal chelate chromatography. The codon-usage optimization involves the inclusion of several codons of extremely rare occurrence in natural E. coli ORFs within a 30 a.a-long N-terminal region. Other codons included in the N-terminus have moderate occurrence in E. coli. The subsequent sequence of the artificial gene has been composed of the most frequently occurring codons in E. coli. The recombinant producer based on the pQE-Nit2 construct allowed purification of the enzyme with an activity of 6.2 ± 0.2 μmol/min/mg protein, which corresponds to or slightly exceeds the specific activity of rat liver Nit2. The omega-amidase preparation is necessary for the screening of potential inhibitors that can be used as candidate drugs to cure hyperammonemia disorders in liver pathologies and oncological diseases.     

Three-step purification of lipopolysaccharide-free, polyhistidine-tagged recombinant antigens of Mycobacterium tuberculosis

Previous work has shown that the study of host immune responses against Mycobacterium tuberculosis, the causative agent of tuberculosis, requires the availability of multiple mycobacterial antigens. Since purification of protein from M. tuberculosis cells is extremely cumbersome, we developed a protocol for purifying milligram amounts of ten recombinant antigens of M. tuberculosis from E. coli cells. Purified proteins were immunologically active and free of contaminants that confound interpretation of cell-based immunological assays. The method utilizes a three-step purification protocol consisting of immobilized metal-chelate affinity chromatography, size exclusion chromatography and anion-exchange chromatography. The first two chromatographic steps yielded recombinant protein free of protein contaminants, while the third step (anion-exchange chromatography) efficiently removed E. coli lipopolysaccharide, a potent polyclonal activator of lymphoid cells. The recombinant proteins were immunologically indistinguishable from their native (i.e., purified from M. tuberculosis) counterparts. Thus the method provides a way to utilize recombinant proteins for immunological analyses that require highly purified antigens.     

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.     

Inhibition of modification and restriction for phages lambda and T-1 by co-infecting T3

Summary The host controlled modifications of phage -DNA byEscherichia coli B, K, and C (P1) can be suppressed by preinfecting the bacteria with UV-irradiated phage T3. Since UV-irradiated T3 induces an enzyme which cleaves S-adenosylmethionine into homoserine and thiomethyl adenosine, and since S-adenosylmethionine is the only methyl group donor for DNA methylation, we conclude that methylation is a required step in the host controlled modification of -DNA.T3 itself successfully infectsE. coli K and B with its nonmethylated DNA. Also, restricted phage or T1 will be accepted by the restrictive hostsE. coli B, K, and C(P1) if these are preinfected with UV-T3. It thus appears that T3 is capable of blocking the restriction mechanisms in these hosts.The inability of T3 to grow on C(P1) is not understood. Since T3-DNA is restricted but not degraded into nucleotides byE. coli C(P1) we presume that degradation is not the initial step in restriction.Supported by Grant No. GB 1033 R of the National Science Foundation.Postdoctoral fellow of the Deutsche Forschungsgemeinschaft.     

A simple method for the purification of over-expressed extracellular sucrase of Zymomonas mobilis from a recombinant Escherichia coli

The over-expressed extracellular sucrase (SacC) of Zymomonas mobilisfrom a recombinant Escherichia coli (pZSP62) carrying the sacC gene was purified partially by repeated cycles of freezing and thawing. This method separated the highly expressed recombinant protein from the bulk of endogenous E. coli proteins. The enzyme was further purified 14 fold with a 55% yield from the cellular extract of E. coli by hydroxyapatite chromatography. The purified enzyme had a Mr of 46 kDa by SDS-PAGE. Its km value for sucrose was 86 mM and was optimal at pH 5.0 and at 36°C.     

Inactivation of Escherichia coli threonine synthase by dl-Z-2-amino-5-phosphono-3-pentenoic acid

The rhizocticines and plumbemicines are two groups of di- and tripeptid antibiotics thought to interfere with threonine or threonine-related metabolism. Z-2-amino-5-phosphono-3-pentenoic acid, the common unusual amino acid constituent of the rhizocticines and plumbemicines, was found to irreversibly inhibit Escherichia coli threonine synthase in a time-dependent reaction that followed pseudo-first order and saturation kinetics. These data provide evidence that the toxicity of the rhizocticines and plumbemicines is due to the inhibition of threonine synthase by Z-2-amino-5-phosphone-3-pentenoic acid, which is liberated by peptidases after uptake into the target cell. Additionally, methods for the purification of threonine synthase from an overproducing E. coli strain and for the enzymatic synthesis of l-homoserine phosphate are described.Abbreviations APPA Z-2-amino-5-phosphono-3-pentenoic acid - HSerP l-homoserine phosphate - PEP phosphoenolpyruvate - PLP pyndoxal 5-phosphate - TS threonine synthase