Intein-mediated protein purification of fusion proteins expressed under high-cell density conditions in E. coli

The intein-mediated purification system has the potential to significantly reduce the recovery costs of industrial recombinant proteins. The ability of inteins to catalyze a controllable peptide bond cleavage reaction can be used to separate a recombinant protein from its affinity tag during affinity purification. Inteins have been combined with a chitin-binding domain to serve as a self-cleaving affinity tag, facilitating highly selective capture of the fusion protein on an inexpensive substrate--chitin (IMPACT) system, New England Biolabs, Beverly, MA). This purification system has been used successfully at a lab scale in low cell density cultures, but has not been examined comprehensively under high-cell density conditions in defined medium. In this study, the intein-mediated purification of three commercially relevant proteins expressed under high-cell density conditions in E. coli was studied. Additionally, losses during the purification process were quantified. The data indicate that the intein fusion proteins expressed under high cell density fermentations were stable in vivo after induction for a significant duration, and the intein fusion proteins could undergo thiol or pH and temperature initiated cleavage reaction in vitro. Thus, the intein-mediated protein purification system potentially could be employed for the production of recombinant proteins at the industrial-scale.     

Self-immobilizing recombinant antibody fragments for immunoaffinity chromatography: generic, parallel, and scalable protein purification

We present the directed immobilization of recombinant antibody fragments as ligands for general immunoaffinity chromatography methods. It is based on fusion proteins of scFv fragments with several chitin-binding domains which can be immobilized directly from a crude bacterial lysate on inexpensive chitin beads for the purification of proteins without any gradient or detector. It has been used with a positive pressure manifold, allowing the parallel processing of 24 different samples on a milligram scale, as convenient as plasmid isolation. The method is demonstrated with several anti-protein antibodies. In addition, methods are presented of using an anti-His tag antibody either alone or directly coupled to IMAC to obtain very pure protein. As those methods are scalable, they should prove very useful in the parallel purification of natural and recombinant proteins on small scales (for proteomics), medium scales (for crystallography and NMR), and very large scales (for therapeutic proteins).     

Intein-mediated one-step purification of Escherichia coli secreted human antibody fragments

In this work, we apply self-cleaving affinity tag technology to several target proteins secreted into the Escherichia coli periplasm, including two with disulfide bonds. The target proteins were genetically fused to a self-cleaving chitin-binding domain-intein tag for purification via a chitin-agarose affinity resin. By attaching the intein-tagged fusion genes to the PelB secretion leader sequence, the tagged target proteins were secreted to the periplasmic space and could be recovered in active form by simple osmotic shock. After chitin-affinity purification, the target proteins were released from the chitin-binding domain tag via intein self-cleaving. This was induced by a small change in pH from 8.5 to 6.5 at room temperature, allowing direct elution of the cleaved target protein from the chitin affinity resin. The target proteins include the E. coli maltose-binding protein and β-lactamase enzyme, as well as two human antibody fragments that contain disulfide bonds. In all cases, the target proteins were purified with good activity and yield, without the need for refolding. Overall, this work demonstrates the compatibility of the ΔI-CM intein with the PelB secretion system in E. coli, greatly expanding its potential to more complex proteins.     

Single-step affinity purification of recombinant proteins using a self-excising module from Neisseria meningitidis FrpC

Purification of recombinant proteins is often a challenging process involving several chromatographic steps that must be optimized for each target protein. Here, we developed a self-excising module allowing single-step affinity chromatography purification of untagged recombinant proteins. It consists of a 250-residue-long self-processing module of the Neisseria meningitidis FrpC protein with a C-terminal affinity tag. The N terminus of the module is fused to the C terminus of a target protein of interest. Upon binding of the fusion protein to an affinity matrix from cell lysate and washing out contaminating proteins, site-specific cleavage of the Asp-Pro bond linking the target protein to the self-excising module is induced by calcium ions. This results in the release of the target protein with only a single aspartic acid residue added at the C terminus, while the self-excising affinity module remains trapped on the affinity matrix. The system was successfully tested with several target proteins, including glutathione-S-transferase, maltose-binding protein, beta-galactosidase, chloramphenicol acetyltransferase, and adenylate cyclase, and two different affinity tags, chitin-binding domain or poly-His. Moreover, it was demonstrated that it can be applied as an alternative to two currently existing systems, based on the self-splicing intein of Saccharomyces cerevisiae and sortase A of Staphylococcus aureus.     

Purification of nucleosidediphosphatase of rat liver by metal-chelate affinity chromatography

A procedure is presented for the purification of nucleosidediphosphatase (nucleosidediphosphate phosphohydrolase, EC 3.6.1.6) of rat liver by affinity chromatography using metal conjugated to epoxy-activated Sepharose 6B. The enzyme is eluted from the conjugate by a solution of L-histidine. The enzyme, when bound to metal-chelate gel, is active in a suspended form, suggesting that the catalytic site is different from the site that binds to the metal-chelate gels. Substrate specificity and Km value of the enzyme obtained are similar to those of the enzyme obtained from the same sources by a conventional procedure, indicating that the metal-chelate affinity chromatography does not bring about any substantial change in the catalytic properties.     

New aspects of isolation and purification of thyroxine-binding globulin from human biological fluids

Based on the new data concerning the multicomponent system of thyroxine-binding proteins in human plasma, some methodological aspects of isolation and purification of thyroxine-binding globulin (TBG) were examined, and a simple two-step procedure for TBG purification was developed. Normal human blood serum, retroplacental serum and amniotic fluid were used as TBG sources. The procedure includes affinity chromatography and adsorption chromatography on a hydroxyapatite column. A biospecific adsorbent was synthesized by stepwise binding of epichlorohydrin and thyroxine to Sepharose. The yield of pure TBG varied from 60 to 80%, depending on the TBG source used. The properties of TBG preparations from retroplacental serum and amniotic fluid were identical; both preparations contained a pregnancy-associated molecular variant, TBG-1. Two novel serum thyroxine-binding proteins were detected, isolated and partly characterized.     

Purification of recombinant membrane proteins tagged with calmodulin-binding domains by affinity chromatography on calmodulin-agarose: example of nicotinamide nucleotide transhydrogenase

This protocol describes affinity purification of bacterially expressed, recombinant membrane proteins fused with calmodulin-binding domains. As exemplified by the Escherichia coli nicotinamide nucleotide transhydrogenase, this method allows isolation of the protein fusions in a single chromatography step using elution with the calcium chelating agent EDTA and, unlike purification of His-tagged proteins on nickel chelate, it is not sensitive to the presence of strong reducing agents (e.g., DTT). Our protocol involves disruption of host bacteria by sonication, sedimentation of membranes by differential centrifugation, solubilization of membrane proteins and affinity chromatography on calmodulin-agarose. To achieve maximum purity and yield, the use of a combination of non-ionic and anionic detergents is suggested. Purification takes two working days, with an overnight wash of the column to increase the purity of the product.     

Metal affinity precipitation of proteins carrying genetically attached polyhistidine affinity tails

In this study, galactose dehydrogenase (EC 1.1.1.48) was chosen as a prototype target protein to investigate the capability of metal affinity precipitation to facilitate the purification of genetically engineered proteins. A DNA fragment encoding five histidine residues was fused to the 3'-terminal end of the galactose dehydrogenase gene from Pseudomonas fluorescens and thereafter expressed in Escherichia coli. The additional five histidines functioned as an affinity tail and the modified enzyme could be purified using metal affinity precipitation when the metal-chelate complex with ethylene glycol-bis-(beta-aminoethyl ether) N,N,N',N'-tetra-acetic acid, EGTA(Zn)2, was added to the protein solution. The affinity tail could also be applied for the purification of the fusion protein utilising immobilised metal affinity chromatography. After purification, the pentahistidine affinity tail could be removed enzymatically by carboxypeptidase A. Furthermore, growth rate experiments demonstrated that the expression of the metal-binding affinity tail in E. coli cells enhanced the tolerance to zinc ions when added to the growth medium.     

Efficient production of active and mutated ADP-ribosyltransferase (S1) of pertussis toxin using affinity expression cassette polymerase chain reaction

Abstract We describe an efficient, general approach for cloning, expression and purification of heterologous proteins in Escherichia coli host strains. The affinity expression cassette polymerase chain reaction (AEC-PCR) allows the insertion of virtually any coding sequence in suitable expression vectors. For ease of purification of the (over)produced protein the gene expression cassettes are engineered by specifically designed oligonucleotide primers in the polymerase chain reaction (PCR) to contain either 3′ or 5′ additional nucleotides coding for a short amino acid sequence constituting an ‘affinity block’ fused to either end of the protein. This allows a one-step purification by affinity chromatography. In combination with PCR-mediated site-specific mutagenesis this approach is a highly efficient way for the expression and isolation of proteins and for the analysis and dissection of functional domains. The application of AEC-PCR is demonstrated by the cloning, production and purification of the native, active and the mutagenized, inactive ADP-ribosyltransferase (S1 subunit) of pertussis toxin. In this example, a string of six histidines has been engineered to either the N-terminal or the C-terminal end of the protein to serve as ‘affinity block’ for the isolation of the recombinant protein by immobilized metal ion affinity chromatography (IMAC). Thus, the S1 subunit can now be produced in sufficient quantities to facilitate further studies on its immunological and molecular properties.     

Affinity chromatography system for parallel purification of recombinant protein samples

In protein engineering, the tasks of generating and testing a large number of variants of a molecule and of optimizing expression conditions for one distinct molecule create the need for purification methods that can handle a large number of samples simultaneously. We describe the development and some application results of a simple affinity chromatography system that can be used for the parallel purification of 24 protein samples, yielding sufficient quantities for biochemical and functional analysis. Advantages of this system over existing systems are as follows. Compared with commercially available complete chromatography systems, the costs of this system are minimal. In comparison with vacuum systems with various outlets, and with batch purification systems where centrifugation is necessary, this system allows gentler processing of the samples. This could be important for proteins that are easily damaged.     

Applications of affinity chromatography in proteomics

Affinity chromatography is a powerful protein separation method that is based on the specific interaction between immobilized ligands and target proteins. Peptides can also be separated effectively by affinity chromatography through the use of peptide-specific ligands. Both two-dimensional electrophoresis (2-DE)- and non-2-DE-based proteomic approaches benefit from the application of affinity chromatography. Before protein separation by 2-DE, affinity separation is used primarily for preconcentration and pretreatment of samples. Those applications entail the removal of one protein or a class of proteins that might interfere with 2-DE resolution, the concentration of low-abundance proteins to enable them to be visualized in the gel, and the classification of total protein into two or more groups for further separation by gel electrophoresis. Non-2-DE-based approaches have extensively employed affinity chromatography to reduce the complexity of protein and peptide mixtures. Prior to mass spectrometry (MS), preconcentration and capture of specific proteins or peptides to enhance sensitivity can be accomplished by using affinity adsorption. Affinity purification of protein complexes followed by identification of proteins by MS serves as a powerful tool for generating a map of protein-protein interactions and cellular locations of complexes. Affinity chromatography of peptide mixtures, coupled with mass spectrometry, provides a tool for the study of protein posttranslational modification (PTM) sites and quantitative proteomics. Quantitation of proteomes is possible via the use of isotope-coded affinity tags and isolation of proteolytic peptides by affinity chromatography. An emerging area of proteomics technology development is miniaturization. Affinity chromatography is becoming more widely used for exploring PTM and protein-protein interactions, especially with a view toward developing new general tag systems and strategies of chemical derivatization on peptides for affinity selection. More applications of affinity-based purification can be expected, including increasing the resolution in 2-DE, improving the sensitivity of MS quantification, and incorporating purification as part of multidimensional liquid chromatography experiments.     

Affinity purification of streptavidin using tobacco mosaic virus particles as purification tags

A new protein affinity purification system has been developed. Recombinant tobacco mosaic virus (TMV) was used as an affinity matrix for isolation and purification of the given protein of interest. In model experiments, streptavidin-specific heptapeptide sequence TLIAHPQ was inserted into TMV coat protein near the C end. This oligopeptide did not interfere significantly with viral replication, assembly, and movement. Recombinant TMV functioned as an epitope tag recognizing streptavidin in plant protein extracts. Plant protein extracts containing streptavidin were incubated with recombinant TMV virions. Affinity complexes of viral particles with the protein of interest were collected by centrifugation. Recombinant TMV-streptavidin complex was dissociated with 0.2M acetic acid, pH 4.6, and was passed through membrane filter Nanosep 300K by centrifugation. The filtrate contained pure streptavidin. Recombinant TMV was left on the filter. TMV particles collected from the filter could be used for at least two more purification cycles. The streptavidin-specific recombinant TMV system was applied successfully for purification of streptavidin from Streptomyces avidinii. The authors believe that the TMV-based affinity system can also be used for the purification of other proteins.     

High-throughput protein purification and quality assessment for crystallization

The ultimate goal of structural biology is to understand the structural basis of proteins in cellular processes. In structural biology, the most critical issue is the availability of high-quality samples. "Structural biology-grade" proteins must be generated in the quantity and quality suitable for structure determination using X-ray crystallography or nuclear magnetic resonance (NMR) spectroscopy. The purification procedures must reproducibly yield homogeneous proteins or their derivatives containing marker atom(s) in milligram quantities. The choice of protein purification and handling procedures plays a critical role in obtaining high-quality protein samples. With structural genomics emphasizing a genome-based approach in understanding protein structure and function, a number of unique structures covering most of the protein folding space have been determined and new technologies with high efficiency have been developed. At the Midwest Center for Structural Genomics (MCSG), we have developed semi-automated protocols for high-throughput parallel protein expression and purification. A protein, expressed as a fusion with a cleavable affinity tag, is purified in two consecutive immobilized metal affinity chromatography (IMAC) steps: (i) the first step is an IMAC coupled with buffer-exchange, or size exclusion chromatography (IMAC-I), followed by the cleavage of the affinity tag using the highly specific Tobacco Etch Virus (TEV) protease; the second step is IMAC and buffer exchange (IMAC-II) to remove the cleaved tag and tagged TEV protease. These protocols have been implemented on multidimensional chromatography workstations and, as we have shown, many proteins can be successfully produced in large-scale. All methods and protocols used for purification, some developed by MCSG, others adopted and integrated into the MCSG purification pipeline and more recently the Center for Structural Genomics of Infectious Diseases (CSGID) purification pipeline, are discussed in this chapter.     

Overexpression and purification of folded domain of prostate cancer related proteins MSMB and PSA

Overexpression of domains of a human protein using recombinant DNA technology has been challenging because individual domains intend to accumulate as non-soluble aggregate when expressed separately. Studies on identifying right sequences for a domain to be able to fold independently may help understand the folding pattern and underlying protein-engineering events to isolate the functional domains of a protein. In this report, individual domains of prostate cancer related biomarkers; MSMB and PSA were overexpressed in bacterial system and purified in their folded forms using affinity chromatography. The western blotting experiment using domain specific antibodies further confirmed these proteins. The designed nucleotide sequences domains were truncated using fold index software and folding were predicted by phyre2 and I-TASSER software. Other parameters were optimized for their overexpression and purification using Co-NTA affinity chromatography. Purified domains of each protein showed secondary structures such as α + β type for PSA, α/β and β type for the each domains of PSA and MSMB respectively. This is the first report on producing PSA and MSMB individual domains in functional folded forms. This study may help produce the folded domain of many such proteins to be used for better diagnostic purpose.     

金黄色葡萄球菌蛋白A (SpA) Z结构域串联体的克隆、表达和筛选

筛选一种高效重组金黄色葡萄球菌蛋白A(SpA)用于制备抗体纯化亲和介质。首先通过基因操作获得金黄色葡萄球菌蛋白A(SpA)的Z结构域单体、二串体、三串体、四串体和五串体基因,将目的基因分别克隆至pET-22b表达载体并转化至大肠杆菌BL21(DE3)感受态细胞,获得不同串联个数的Z结构域基因工程菌,经诱导表达和Ni2+亲和层析纯化得到Z结构域单体和二-五串体蛋白。纯化后的目的蛋白偶联至琼脂糖凝胶作为亲和层析介质,对人免疫球蛋白G(IgG)进行分离纯化。分析比较Z结构域串联体蛋白产量及其偶联的亲和介质对抗体吸附载量的差异。结果表明,构建的Z结构域单体、二串体、三串体、四串体和五串体基因工程菌能有效表达目的蛋白,制备的凝胶亲和介质可特异性吸附人IgG。增加Z结构域串联数,重组蛋白产量和单位摩尔数多聚体蛋白吸附载量获得提高,其中,重组四串体蛋白产量大(160 mg/10 g湿菌体),对抗体的吸附载量高(34.4 mg人IgG/mL胶),更适合作为配基用于亲和层析介质的制备。     

Sequential isolation of superoxide dismutase and ajmaline from a tissue culture of Rauwolfia serpentina Benth

Two biologically active compounds, the enzyme superoxide dismutase (EC 1.15.1.1) and the antiarrhythmic indole alkaloid ajmaline, were isolated from a callus culture of Rauwolfia serpentina Benth. Sequential isolation of biologically active compounds by metal-chelate affinity chromatography followed by azoadsorbent affinity chromatography allowed us to obtain highly purified products. The yields of superoxide dismutase and ajmaline were 180 mg/kg biomass and 16.5 g/kg dry weight, respectively.     

Isolation,purification, and study of properties of recombinant hepsin from <Emphasis Type="Italic">Escherichia coli</Emphasis>

A recombinant hepsin-producing strain of Escherichia coli was obtained and the conditions for hepsin expression in a bacterial system were optimized. To study the physicochemical properties of the enzyme, a procedure for purification of active recombinant hepsin using metal-chelate affinity chromatography and ion-exchange chromatography was developed. The interaction of recombinant hepsin with various peptide substrates is characterized. The dose-dependent inhibition of the recombinant hepsin enzyme activity by anthralin in vitro and an increase in the hepsin enzymatic activity in the presence of resveratrol were revealed.     

Development of a purification procedure for the placental protein 14 involving metal-chelate affinity chromatography and hydrophobic interaction chromatography

Placental protein 14 was isolated from the biological material of patients undergoing legal abortions. The major part of ballast protein was removed by ion-exchange chromatography on DEAE-Sepharose and CM-Sepharose. Albumin was separated by chromatography on Blue-Sepharose. Complete purification was obtained by metal-chelate affinity chromatography on Nickel-Chelate Sepharose and hydrophobic interaction chromatography on Phenyl-Sepharose and Octyl-Sepharose. The protein was not exposed to denaturing agents or extreme pH.     

Protein engineering to optimize recombinant protein purification

Genetic approaches have been used to facilitate purification of recombinant proteins, on both a large and a small scale. Based on developments in three different areas: (i) affinity chromatography; (ii) specific cleavage of fusion proteins and (iii) secretion of fusion proteins, a coupled expression/secretion system was designed. It was further improved by protein engineering. Using a synthetic DNA fragment, encoding two IgG-binding domains derived from staphylococcal protein A, gene products were secreted to the culture medium of Escherichia coli and purified with a one-step affinity procedure. The system has been used for large-scale production of biologically active human peptide hormones, to generate peptides for antibody production and to immobilize proteins on solid supports.