Screening of suitable immobilized metal chelates for adsorption of monoclonal antibodies against mutant amidase from Pseudomonas aeruginosa

The chromatographic behaviour of monoclonal antibodies (MAbs) of IgM class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated. The effect of ligand concentration, the length of spacer arm and the nature of metal ion were investigated on immobilized metal ion affinity chromatography (IMAC). MAbs against mutant amidase adsorbed to Cu (II), Ni (II), Zn (II), Co (II) and Ca (II)-IDA agarose columns. The adsorption of MAbs onto immobilized metal chelates was pH dependent because an increase in the binding of MAbs was observed as the pH was raised from 6.0 to 8.0. The adsorption of MAbs to metal chelates was due to coordination of histidine residues which are available in the 3rd constant domain of heavy chain (CH3) of immunoglobulins since the presence of imidazole in the equilibration buffer abolished the adsorption of MAbs to the column packed with commercial IDA-Zn(II) agarose at pH 8.0. The combination of tailor-made stationary phases for IMAC and a correct choice of the adsorption conditions permitted to design a one-step purification procedure for MAbs of IgM class. Culture supernatants containing MAbs of IgM class against mutant amidase (T103I) were chromatographed by IMAC Co (II) column at pH 8.0. The results strongly suggest that one-step purification of MAbs of IgM class by IMAC is a cost-effective and process-compatible alternative to the other purification procedures.     

Immobilized metal affinity chromatography of monoclonal immunoglobulin M against mutant amidase from Pseudomonas aeruginosa

The chromatographic behavior of monoclonal antibodies (MAbs) of immunoglobulin (Ig) M class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated on immobilized metal chelates. The effect of ligand concentration, the length of spacer arm, and the nature of metal ion were investigated in immobilized metal affinity chromatography (IMAC). The MAbs against mutant amidase adsorbed to Cu(II), Ni(II), Zn(II), Co(II), and Ca(II)-iminodiacetic acid (IDA) agarose columns. The increase in ligand concentration (epichlorohydrin: 30-60 and 1,4-butanediol-diglycidyl ether: 16-36) resulted in higher adsorption to IgM into immobilized metal chelates. The length of spacer arm was found to affect protein adsorption, as longer spacer arm (i.e., 1,4-butanediol-diglycidyl ether) increased protein adsorption of immobilized metal chelates. The adsorption of IgM onto immobilized metal chelates was pH dependent because an increase in the binding of IgM was observed as the pH varied from 6.0 to 8.0. The adsorption of IgM to immobilized metal chelates was the result of coordination of histidine residues to metal chelates that are available in the third constant domain of heavy chain (CH3) of immunoglobulins, as the presence of imidazole (5 mM) in the equilibration buffer abolished the adsorption of IgM to the column. The combination of tailor-made stationary phases for IMAC and a correct design of the adsorption parameters permitted to devise a one-step purification procedure for IgM. Culture supernatants containing IgM against mutant amidase (T103I) were purified either by IMAC on EPI-60-IDA-Co (II) column or by gel filtration chromatography on Sephacryl S-300HR. The specific content of IgM and final recovery of antibody activity exhibited similar values for both purification schemes. The purified preparations of IgM obtained by both schemes were apparently homogeneous on native polyacrylamide gel electrophoresis with a Mr of 851,000 Da. The results presented in this work strongly suggest that one-step purification of IgM by IMAC is a cost-effective and processcompatible alternative to other types of chromatography.     

Immobilized metal affinity chromatography of monoclonal immunoglobulin M against mutant amidase from Pseudomonas aeruginosa

The chromatographic behavior of monoclonal antibodies (MAbs) of immunoglobulin (Ig) M class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated on immobilized metal chelates. The effect of ligand concentration, the length of spacer arm, and the nature of metal ion were investigated in immobilized metal affinity chromatography (IMAC). The MAbs against mutant amidase adsorbed to Cu(II), Ni(II), Zn(II), Co(II), and Ca(II)-iminodiacetic acid (IDA) agarose columns. The increase in ligand concentration (epichlorohydrin: 30–60 and 1,4-butanediol-diglycidyl ether: 16–36) resulted in higher adsorption to IgM into immobilized metal chelates. The length of spacer arm was found to affect protein adsorption, as longer spacer arm (i.e., 1,4-butanediol-diglycidyl ether) increased protein adsorption of immobilized metal chelates. The adsorption of IgM onto immobilized metal chelates was pH dependent because an increase in the binding of IgM was observed as the pH varied from 6.0 to 8.0. The adsorption of IgM to immobilized metal chelates was the result of coordination of histidine residues to metal chelates that are available in the third constant domain of heavy chain (CH3) of immunoglobulins, as the presence of imidazole (5 mM) in the equilibration buffer abolished the adsorption of IgM to the column. The combination of tailor-made stationary phases for IMAC and a correct design of the adsorption parameters permitted to devise a one-step purification procedure for IgM. Culture supernatants containing IgM against mutant amidase (T103I) were purified either by IMAC on EPI-60-IDA-Co (II) column or by gel filtration chromatography on Sephacryl S-300HR. The specific content of IgM and final recovery of antibody activity exhibited similar values for both purification schemes. The purified preparations of IgM obtained by both schemes were apparently homogeneous on native polyacrylamide gel electrophoresis with a M _r of 851,000 Da. The results presented in this work strongly suggest that one-step purification of IgM by IMAC is a cost-effective and process-compatible alternative to other types of chromatography.     

Purification of carboxypeptidase B by metal chelation affinity chromatography.

Norwegian lobster carboxypeptidase B (CPB) was purified in one step using immobilized metal chelate affinity chromatography (IMAC). The separation is based on the property that CPB has a high affinity for metal ions such as Cu2+. The CPB was purified from an hepatopancreas extract containing several endo- and exo-proteolytic activities. Its homogeneity was demonstrated by SDS-electrophoresis and isoelectric focusing in immobilized pH gradients. The implication of hydrophobic interaction between this enzyme and the IDA-Cu2+ gel is postulated.     

Homologous human blood protein separation using immobilized metal affinity chromatography: protein C separation from prothrombin with application to the separation of factor IX and prothrombin.

Protein C (PC) is a natural anticoagulant and antithrombotic present in human blood at a concentration of 4 microg/mL. Its deficiency can result in excessive clotting and thrombosis. Protein C can be obtained from human blood plasma; however, there are other coagulant proteins in blood, including prothrombin (factor II), which is present in relatively large amounts and is one of the most active components. Protein C and prothrombin are homologous proteins with similar biochemical features; therefore, immunoaffinity chromatography is used for their separation. However, this technology is very expensive, protein C recovery and activity is low, and contamination problems with mouse antibody are likely. Immobilized metal affinity chromatography (IMAC) utilizes the protein metal-binding properties for protein separation. Protein C has twelve surface-accessible histidines, which are the major metal-binding groups for IMAC separation. After investigating metal ion-binding properties of protein C, we used an IDA-Cu column to separate protein C and prothrombin. Following protein adsorption to the column, prothrombin was washed out using a sodium phosphate buffer containing 2 mM imidazole and protein C was recovered with 15 mM imidazole in the buffer. The mild elution condition allows a high protein C activity and a high recovery. Also, this technology introduces no immunoglobulins, and it is relatively inexpensive. IMAC could replace the immunoaffinity technology for the large-scale separation of protein C from blood plasma Cohn Fraction IV-1. In addition, this work demonstrates a significant application of this technology for the separation of factor IX from prothrombin. Prothrombin has proven to be a harmful contaminant in factor IX cocktails that have been administered to humans in the treatment of hemophilia B.     

Immobilized palladium(II) ion affinity chromatography for recovery of recombinant proteins with peptide tags containing histidine and cysteine

Fusion of peptide‐based tags to recombinant proteins is currently one of the most used tools for protein production. Also, immobilized metal ion affinity chromatography (IMAC) has a huge application in protein purification, especially in research labs. The combination of expression systems of recombinant tagged proteins with this robust chromatographic system has become an efficient and rapid tool to produce milligram‐range amounts of proteins. IMAC‐Ni(II) columns have become the natural partners of 6xHis‐tagged proteins. The Ni(II) ion is considered as the best compromise of selectivity and affinity for purification of a recombinant His‐tagged protein. The palladium(II) ion is also able to bind to side chains of amino acids and form ternary complexes with iminodiacetic acid and free amino acids and other sulfur‐containing molecules. In this work, we evaluated two different cysteine‐ and histidine‐containing six amino acid tags linked to the N‐terminal group of green fluorescent protein (GFP) and studied the adsorption and elution conditions using novel eluents. Both cysteine‐containing tagged GFPs were able to bind to IMAC‐Pd(II) matrices and eluted successfully using a low concentration of thiourea solution. The IMAC‐Ni(II) system reaches less than 20% recovery of the cysteine‐containing tagged GFP from a crude homogenate of recombinant Escherichia coli, meanwhile the IMAC‐Pd(II) yields a recovery of 45% with a purification factor of 13. Copyright © 2014 John Wiley & Sons, Ltd.     

Immobilized metal-ion affinity chromatography of human antibodies and their proteolytic fragments

Immobilized metal-ion affinity chromatography (IMAC) performed with four different transition metal ions: copper(II), nickel(II), zinc(II) and cobalt(II), was used to study the adsorption properties of human polyclonal gamma-globulines (IgG), Cohn II-III fractions, and their pepsin cleaved fragments: Fab'2 and F'c. In each case, digested products showed lower affinity for metal ions, as well by decreasing pH elution as by competition with imidazole. An explanation was proposed by the presence of a histidine (His) cluster in the F'c domain of IgGs, identified by computer calculation (accessible surface area (ASA) determination) as the more probable His 433-x-His 435 sequence presented in the CH3 domain of human IgG heavy chain. As shown by IMAC and electrophoresis, F'c and undigested IgG have higher affinity for transition metal ions than Fab'2 fragments and could be then separated in one step by IMAC. When chelated Zn(II) or Co(II) are used as ligands, the Fab'2 fragment could be easily recovered under mild conditions (pH 7) in the non-retained fraction. This approach could be used as a powerful alternative to conventional protein A/G methods for the commercial preparation of non immunogen active Fab'2 fragments.     

Two-step method to isolate target recombinant protein from co-purified bacterial contaminant SlyD after immobilised metal affinity chromatography

As part of a study to purify the internal domain of HER2 (ICD) from recombinant expression, through metal immobilised affinity chromatography (IMAC), we encountered a contaminant, SlyD, a 29 kDa native E. coli protein. SlyD is a recurrent contaminant, with a histidine rich domain enabling binding to IMAC columns and thus co-elution with the target protein. Research has been carried out on this protein and its purification, however, no work mentions how to treat it as a true contaminant or describe procedures to isolate it from target proteins. In this report, we described a two-step chromatographic method for the purification of ICD, including IMAC as a capture step and size exclusion chromatography (SEC) as a polishing step. IMAC allowed us to purify ICD from bacterial crude with SlyD co-eluting. SEC then allowed us to resolve ICD from SlyD and achieve a purity greater than 95% for ICD. However, this method has been developed to accommodate any protein whose molecular weight is different enough from SlyD to be separated by SEC.     

Structure-function relationship in glycosylated alpha-chymotrypsin as probed by IMAC and IMACE.

Chemical glycosylation of bovine alpha-chymotrypsin, by a glucosamine adduct on the carboxyl group, results in the modification of its catalytic activity. The structural alterations of alpha-chymotrypsin resulting from its glycosylation are studied by immobilized metal-ion affinity chromatography (IMAC) and immobilized metal-ion affinity capillary electrophoresis (IMACE). The chemical glycosylation of alpha-chymotrypsin generates two distinct subpopulations of the protein: one which totally loses the initial affinity for IDA-Cu(II) and another which exhibits an increased affinity for the metal chelate ligand.     

金属螯合亲和层析分离蛋白质的研究

金属螯合亲和层析是近20年发展起来的一项新型分离技术。它以配基简单、吸附量大、分离条件温和、通用性强等特点,逐渐成为分离纯化蛋白质等生物工程产品最有效的技术之一。本文从单组分蛋白质入手,考查了pH值、铵离子浓度、不同铵盐等对蛋白质洗脱的影响,并进行了分析。还对不同的金属螯合柱和不同性质蛋白质的洗脱性能进行了研究,比较了不同金属离子与蛋白质亲和力的区别,为实际体系的分离研究打下了基础。     

Purification of a catalase from Thermus thermophilus via IMAC chromatography: effect of the support

A hexameric Mn-catalase was purified from crude extracts of Thermus thermophilus using ammonium sulfate precipitation and ion metal-chelate affinity chromatography (IMAC). Eupergit 250 and Sepabeads FP-EP3 epoxy supports derivatized with iminodiacetic acid (IDA) and copper were used, at similar micromole/packed milliliter of support. Although Eupergit 250-IDA-Cu support adsorbed 80% of the total proteins in the extract, it exhibited a minimum affinity for the catalase. On the other hand, Sepabeads FP-EP3-IDA-Cu allowed the full adsorption of the catalase activity, which could be desorbed in fractions of different purity. This was attributed to a different geometrical congruence of the support surfaces with the enzyme surface, resulting in a different ability to form multipoint interactions with the proteins. Thus, by a cleanup step, followed by a negative chromatographic step using Eupergit 250-IDA-Cu2+ and by the adsorption of the catalase on Sepabeads-IDA-Cu2+ support, a pure enzyme fraction was obtained and its N-terminal end was sequenced.     

Preparative separation of small molecular weight peptides from casein hydrolysate using gel filtration and immobilized metal ion affinity chromatography

A two step method consisting of a gel filtration step, followed by a Immobilized Metal Affinity Chromatography (IMAC) step using a IDA-Cu coupled Sephadex G-25 column, on a preparative scale is described for the group separation of peptides from a casein hydrolysate. The 48 groups of peptides thus separated are further characterised by RP-HPLC and amino acid analysis. Some peptides after the analytical RP-HPLC step are further characterised by sequencing. An insight into the mechanism of retention on IMAC of the peptides is attempted. In such complex mixtures as casein hydrolysate, the peptide-peptide interaction can mask the potential sites of interactions in a single peptide. The results obtained using volatile buffers as eluents show the possibility of using IMAC step as an alternative to obtain gram quantities of group of peptides free of salts from complex protein hydrolysates.     

Recovery and purification of aprotinin from industrial insulin-processing effluent by immobilized chymotrypsin and negative IMAC chromatographies

Aprotinin, a bovine protease inhibitor currently also produced in recombinant bacteria, yeast, and corn, has valuable applications as a human therapeutic and in tissue culture. The objective of this work was to develop the basis of a large-scale aprotinin purification process centered on immobilized metal ion affinity chromatography (IMAC). This technique uses ligands—metal ions—of a lower cost and higher stability than those traditionally used in affinity chromatography. Since aprotinin does not interact with IMAC ligands, collection is from the nonretained fractions (negative chromatography). Stirred-tank batch IMAC adsorption experiments indicated that one-step aprotinin purification could not be successful. Immobilized chymotrypsin chromatography was then used as a prepurification step, yielding a suitable feed for IMAC (with purification factors as high as 476). IMAC column fed with these prepurified materials produced purified aprotinin in the nonretained fractions with purification factors as high as 952.     

A recombinant envelope protein from Dengue virus purified by IMAC is bioequivalent with its immune-affinity chromatography purified counterpart.

Semi-purified DEN-4 envelope protein, obtained in Pichia pastoris, was capable of generating neutralising and protecting antibodies after immunisation in mice. Here we compared two purification processes of this recombinant protein using two chromatographic steps: immune-affinity chromatography and immobilised metal ion adsorption chromatography (IMAC). The protein purified by both methods produced functional antibodies reflected by titres of haemagglutination inhibition and neutralisation. IMAC could be used as an alternative for high scale purification.     

Development of metal affinity-immobilized liposome chromatography and its basic characteristics

Metal affinity-immobilized liposome chromatography (MA-ILC) was newly developed as a chromatographic technique to separate and analyze peptides. The MA-ILC matrix gel was first prepared by immobilizing liposomes modified with functional ligands. The functional ligand used to adsorb metal ions was N-hexadecyl iminodiacetic acid (HIDA), which is obtained by attaching a long alkyl chain to an iminodiacetic acid (IDA). Cu(II) ion was first adsorbed on the gel matrix through its complex formation with the HIDA on the surface of the immobilized liposome. Synthetic peptides of various types ranging in size from 5 to 40 residues were then used, and their retention properties on the MA-ILC were evaluated. The retention property of peptides on the MA-ILC by using a usual imidazole elution was compared with the retention property in the case of the immobilized metal affinity chromatography (IMAC) and an immobilized liposome chromatography (ILC). It was found that the retention property of peptides on the MA-ILC has the features of both the IMAC and the ILC; the retention ability of peptides depends on both the number of histidine residues in peptides and the liposome membrane affinity of the peptides. Histidine and tryptophan residues among amino acid residues in peptides indicated a high contribution coefficient for the peptide retention on the MA-ILC, probably due to their metal ion and membrane interaction properties, respectively.     

Chromatographic behaviour of glucose 1- and 2-oxidases from fungal strains on immobilized metal chelates

Glucose 2-oxidase (EC 1.1.3.10) from Coriolus versicolor and Phanerochaete chrysosporium and glucose 1-oxidase (EC 1.1.3.4) from Aspergillus niger bound to a CU(II)-IDA column in the pH range of 6–8. However, glucose 1-oxidase from Penicillium amagasakiense bound only partially to a CU(II)-IDA column at pH 8.0. Metal chelates containing either Ni(II) or Zn(II) were useful in the adsorption of glucose 2-oxidase from Phanerochaete chrysosporium. The binding of glucose 2-oxidase from P. chrysosporium to Ni(II) and Zn(II)-IDA agarose columns increases as a function of pH of the buffer system. The adsorption of glucose oxidases on metal(II)-IDA chelates was due to the available histidine residues on enzyme molecules since the addition of imidazole in the buffer system abolished the binding of glucose oxidases to these columns. Both glucose oxidases from C.versicolor, P. chrysosporium and A. niger were purified in one step by immobilized metal affinity chromatography on metal(II)-IDA agarose columns with a recovery of enzyme activity in the range of 80–91%. Purified preparations of glucose oxidases from fungal strains were apparently homogeneous on native PAGE and SDS-PAGE. Immobilized metal affinity chromatography was used to separate glucose 1-oxidase from the 2-oxidase on metal(II)-IDA agarose columns which was confirmed by analysis of the reaction products by HPLC. The different chromatographic behaviour of glucose oxidases on metal(II)-IDA chelates is apparently due to the number and spatial distribution of available histidine residues on these enzyme molecules. Received 12 May 1998/ Accepted in revised form 29 July 1998     

A modified IMAC method for the capture of target protein from mammalian cell culture harvest containing metal chelating species

Although immobilized metal affinity chromatography (IMAC) offers high capacity and protein selectivity it is not typically used commercially for the capture of native proteins from mammalian cell culture harvest. This is due mainly to the potential for low target recovery due to the presence of strong metal ion chelating species in the harvest that compete for the metal immobilized on the resin. To address this issue a buffer exchange step, such as tangential flow filtration (TFF), is added after harvest clarification and prior to IMAC to remove the interfering harvest components. The addition of a TFF step adds process time and cost and reduces target protein recovery. The elimination of the TFF might make IMAC competitive with other orthogonal methods of protein capture. In this study, we developed a modified IMAC method to allow the direct loading of clarified mammalian harvest without prior buffer exchange (direct IMAC). Although the target enzyme recovery was lower than that from standard IMAC the elimination of the buffer exchange step resulted in a 19% increase in overall enzyme recovery. The target enzyme capacity in direct IMAC was higher, in our experience, than the capacity of hydrophobic interaction (HIC) and ion-exchange (IEX) for protein capture. An economic evaluation of using direct IMAC as a capture step in manufacturing is also discussed.     

Production of polygalacturonase from <Emphasis Type="Italic">Coriolus versicolor</Emphasis> grown on tomato pomace and its chromatographic behaviour on immobilized metal chelates

Tomato pomace and pectin were used as the sole carbon sources for the production of polygalacturonase from a strain of Coriolus versicolor in submerged culture. The culture of C. versicolor grown on tomato pomace exhibited a peak of polygalacturonase activity (1,427 U/l) on the third day of culture with a specific activity of 14.5 U/mg protein. The production of polygalacturonase by C. versicolor grown on pectin as a sole carbon source increased with the time of cultivation, reaching a maximum activity of 3,207 U/l of fermentation broth with a specific activity of 248 U/mg protein. The levels of different isoenzymes of polygalacturonase produced during the culture growth were analysed by native PAGE. Differential chromatographic behaviour of lignocellulosic enzymes produced by C. versicolor (i.e. polygalacturonase, xylanase and laccase) was studied on immobilized metal chelates. The effect of ligand concentration, pH, the length of spacer arm and the nature of metal ion were studied for enzyme adsorption on immobilized metal affinity chromatography (IMAC). The adsorption of these lignocellulosic enzymes onto immobilized metal chelates was pH-dependent since an increase in protein adsorption was observed as the pH was increased from 6.0 to 8.0. The adsorption of polygalacturonase as well as other enzymes to immobilized metal chelates was due to coordination of histidine residues which are available at the protein surface since the presence of imidazole in the equilibration buffer abolished the adsorption of the enzyme to immobilized metal chelates. A one-step purification of polygalacturonase from C. versicolor was devised by using a column of Sepharose 6B-EPI 30-IDA-Cu(II) and purified enzyme exhibited a specific activity of about 150 U/mg protein, final recovery of enzyme activity of 100% and a purification factor of about 10. The use of short spacer arm and the presence of imidazole in equilibration buffer exhibited a higher selectivity for purification of polygalacturonase on this column with a high purification factor. The purified enzyme preparation was analysed by SDS-PAGE as well as by "in situ" detection of enzyme activity.     

Rapid purification of the potato ADP-glucose pyrophosphorylase by polyhistidine-mediated chromatography

In an attempt to obtain facile methods to purify the heterotetrameric ADP-glucose pyrophosphorylase (AGPase), polyhistidine tags were attached to either the large (LS) or small (SS) subunits of this oligomeric enzyme. The addition of polyhistidine tag to the N-terminus of the LS or SS and co-expression with its unmodified counterpart subunit resulted in substantial induction of enzyme activity. In contrast, attachment of a polyhistidine-containing peptide through the use of a commercially available pET vector or addition of polyhistidine tags to the C-terminal ends of either subunit resulted in poor expression and/or production of enzyme activity. Preliminary experiment showed that these polyhistidine N-terminal-tagged enzymes interacted with Ni-NTA-agarose, indicating that immobilized metal affinity chromatography (IMAC) would be useful for efficient purification of the heterotetrameric AGPases. When ion-exchange chromatography step was employed prior to the IMAC, the polyhistidine-tagged AGPases were purified to near homogeneity. Comparison of kinetic parameters between AGPases with and without the polyhistidine tags revealed that attachment of the polyhistidine did not alter the allosteric and catalytic properties of the enzymes. These results indicate that polyhistidine tags will be useful for the rapid purification of preparative amounts of AGPases for biochemical and physical studies.     

Interactions of proteins with immobilized metal ions: a comparative analysis using various isotherm models

Immobilized metal ion affinity chromatography (IMAC) is now a widely accepted technique for the purification of natural and recombinant therapeutic products and is beginning to find industrial applications. The design, optimization, and scale-up of a chromatographic process using IMAC demands a thorough understanding to be developed regarding the fundamental factors governing the various interactions between immobilized metal ions and proteins. Consequently, there is an immediate need to find out a theory that is able to account for these interactions most efficiently in a qualitative as well as a quantitative manner. In view of this requirement, the interactions of several model proteins (lysozyme, ovalbumin, bovine serum albumin, conalbumin, and wheat germ agglutinin) with metal (Cu(II), Ni(II))-chelated IDA (iminodiacetate) and tris(2-aminoethyl)amine were investigated. The adsorption data were analyzed using four isotherm models, viz., the general affinity interaction theory/Langmuir model, the Freundlich model, the Temkin model, and the Langmuir-Freundlich model, and the sorption parameters were computed. Although the first three models were applicable to some protein-IMA-M(II) systems, the Langmuir-Freundlich model appeared to be the most efficient model for explaining the interactions of proteins with IMA-M(II) gels. Also, this model was able to explain cooperativity and binding heterogeneity in quantitative terms. It is envisaged that this analysis would be useful in developing an improved understanding of protein-immobilized metal ion interactions and providing guidelines for designing preparative-scale separations using IMAC.