Rapid affinity purification of erythropoietin from biological samples using disposable monoliths.

Identification of post-translational modifications of proteins in biological samples often requires access to preanalytical purification and concentration methods. In the purification step high or low molecular weight substances can be removed by size exclusion filters, and high abundant proteins can be removed, or low abundant proteins can be enriched, by specific capturing tools. In this paper is described the experience and results obtained with a recently emerged and easy-to-use affinity purification kit for enrichment of the low amounts of EPO found in urine and plasma specimens. The kit can be used as a pre-step in the EPO doping control procedure, as an alternative to the commonly used ultrafiltration, for detecting aberrantly glycosylated isoforms. The commercially available affinity purification kit contains small disposable anti-EPO monolith columns (6 ?L volume, Ø7 mm, length 0.15 mm) together with all required buffers. A 24-channel vacuum manifold was used for simultaneous processing of samples. The column concentrated EPO from 20 mL urine down to 55 ?L eluate with a concentration factor of 240 times, while roughly 99.7% of non-relevant urine proteins were removed. The recoveries of Neorecormon (epoetin beta), and the EPO analogues Aranesp and Mircera applied to buffer were high, 76%, 67% and 57%, respectively. The recovery of endogenous EPO from human urine was 65%. High recoveries were also obtained when purifying human, mouse and equine EPO from serum, and human EPO from cerebrospinal fluid. Evaluation with the accredited EPO doping control method based on isoelectric focusing (IEF) showed that the affinity purification procedure did not change the isoform distribution for rhEPO, Aranesp, Mircera or endogenous EPO. The kit should be particularly useful for applications in which it is essential to avoid carry-over effects, a problem commonly encountered with conventional particle-based affinity columns. The encouraging results with EPO propose that similar affinity monoliths, with the appropriate antibodies, should constitute useful tools for general applications in sample preparation, not only for doping control of EPO and other hormones such as growth hormone and insulin but also for the study of post-translational modifications of other low abundance proteins in biological and clinical research, and for sample preparation prior to in vitro diagnostics.

Affinity purification of 61- and 65-kDa rat brain corticotropin-releasing factor receptors and receptor-associated G proteins.

Corticotropin-releasing factor (CRF) has been shown to have a central role in physiological adaptation to stress. It is recognized for stimulating the release of adrenocorticotropin from the anterior pituitary gland, and has more recently been implicated as a regulator of autonomic and immunological responses to stress. Much confusion has surrounded the characterization of CRF receptors, with proteins of varying molecular weights having been identified but never purified and characterized. Recently, two CRF receptors have been cloned from brain and pituitary gland, but evidence from in-situ hybridization studies suggests that further CRF receptor types exist. We therefore developed two techniques which enable the isolation of CRF receptors from whole rat brain. The use of a solid-phase CRF analogue affinity column and elution using a competing ligand resulted in the purification of a single protein of 61 kDa. A second technique was devised which allowed the co-isolation of associated signalling proteins and the identification of CRF bound species following purification. CRF was covalently cross-linked to receptors and the complex purified using antibodies specific for the ligand. This enabled the purification of a CRF receptor of approximately 65 kDa and associated alpha and beta gamma G protein subunits. This study demonstrates the successful isolation of CRF receptors which are of different molecular weights to those previously observed from affinity cross-linking studies or predicted from cloned genes. In addition, we confirm the involvement of G proteins in CRF stimulated cell signalling by demonstrating their association with purified CRF receptor.

DIAGNOSTIC ANTIGENS FOR SCHISTOSOMIASIS MANSONI: PRODUCTION, CHARACTERIZATION AND PURIFICATION OF MONOCLONAL ANTIBODIES, AND AFFINITY PURIFICATION OF ANTIGENS

Attempts have been made in this dissertation to develop a purified antigen with high sensitivity and specificity for diagnosis of Schistosoma mansoni (Sm) infection by using the hybridoma technique.^ Spleen cells, obtained from mice immunized by infection with Sm and boosted by cercarial antigens, or by injection of circulating antigen (CA) in serum from infected mice, were fused with Sp2/0 myeloma cells. The active infection resulted a higher number of hybridomas (100%) than by CA (20%), and higher levels of antibody reactivity as measured by ELISA.^ The IgM and IgG monoclonal antibodies (MCAbs) were purified respectively by gel filtration, DE 52 ion exchange column and proteinase A affinity column. The cercarial and egg antigens were purified by affinity chromatography through MCAb/affi-gel column. The reactivity of the purified antigens were then monitored by ELISA, SDS-PAGE silver stain and EITB.^ The respective MCAbs recognized varying antigenic determinants (AD) present in adult, cercaria and egg stages. By EITB the MCAbs IgM and IgG, when reacted with nine antigens from the various stages, revealed identical bands, suggesting that the two MCAb classes originated from identical AD. By ELISA and COPT, the MCAbs from thirteen cell lines gave same results. But by CHR, two MCAbs showed negative results while eleven other MCAbs showed strong positive. It is assumed that the AD in the immunogen that ilicited the MCAbs were immunochemically closely related.^ One egg purified by immunoaffinity indicated that the epitopes recognized by MCAb were present on four antigenic components with molecular weights (Mr) of approximately 19, 25, 60 and >224 kd, respectively. By EITB the Mr 19 doublet appeared to be species specific; the Mr 25 kd genus specific. They reacted with mouse serum from 13-16 weeks after infection. In monkey serum Mr 19 doublet appeared 8-10 weeks after infection and disappeared at 8-12 weeks after Droncit treatment, paralleled to the disappearance of fecal egg. The Mr 60 and >224 kd bands were also demonstrated with S. japonicum, S. haematobium and Trichinella spiralis infection sera and may be the cause of cross-reaction in conventional serological test. ^

A novel multiple affinity purification tag and its use in identification of proteins associated with a cyclin–CDK complex

A novel multiple affinity purification (MAFT) or tandem affinity purification (TAP) tag has been constructed. It consists of the calmodulin binding peptide, six histidine residues, and three copies of the hemagglutinin epitope. This ‘CHH’ MAFT tag allows two or three consecutive purification steps, giving high purity. Active Clb2–Cdc28 kinase complex was purified from yeast cells after inserting the CHH tag into Clb2. Associated proteins were identified using mass spectrometry. These included the known associated proteins Cdc28, Sic1 and Cks1. Several other proteins were found including the 70 kDa chaperone, Ssa1.

Sephadex-binding RNA ligands: rapid affinity purification of RNA from complex RNA mixtures

Sephadex-binding RNA ligands (aptamers) were obtained through in vitro selection. They could be classified into two groups based on their consensus sequences and the aptamers from both groups showed strong binding to Sephadex G-100. One of the highest affinity aptamers, D8, was chosen for further characterization. Aptamer D8 bound to dextran B512, the soluble base material of Sephadex, but not to isomaltose, isomaltotriose and isomaltotetraose, suggesting that its optimal binding site might consist of more than four glucose residues linked via α-1,6 linkages. The aptamer was very specific to the Sephadex matrix and did not bind appreciably to other supporting matrices, such as Sepharose, Sephacryl, cellulose or pustulan. Using Sephadex G-100, the aptamer could be purified from a complex mixture of cellular RNA, giving an enrichment of at least 60 000-fold, compared with a non-specific control RNA. These RNA aptamers can be used as affinity tags for RNAs or RNA subunits of ribonucleoproteins to allow rapid purification from complex mixtures of RNA using only Sephadex.

LacI-mediated sequence-specific affinity purification of plasmid DNA for therapeutic applications

Affinity purification of plasmid DNA is an attractive option for the biomanufacture of therapeutic plasmids, which are strictly controlled for levels of host protein, DNA, RNA, and endotoxin. Plasmid vectors are considered to be a safer alternative than viruses for gene therapy, but milligram quantities of DNA are required per dose. Previous affinity approaches have involved triplex DNA formation and a sequence-specific zinc finger protein. We present a more generically applicable protein-based approach, which exploits the lac operator, present in a wide diversity of plasmids, as a target sequence. We used a GFP/His-tagged Lacl protein, which is precomplexed with the plasmid, and the resulting complex was immobilized on a solid support (TALON resin). Ensuing elution gives plasmid DNA, in good yield (>80% based on recovered starting material, 35-50% overall process), free from detectable RNA and protein and with minimal genomic DNA contamination. Such an affinity-based process should enhance plasmid purity and ultimately, after appropriate development, may simplify the biomanufacturing process of therapeutic plasmids.

Affinity purification of plasmid DNA directly from crude bacterial cell lysates

We have shown previously that a sequence-specific DNA-binding protein based on the Lac repressor protein can isolate pre-purified DNA efficiently from simple buffer solution but our attempts to purify plasmids directly from crude starting materials were disappointing with unpractically low DNA yields. We have optimized tbe procedure and present a simple affinity methodology whereby plasmid DNA is purified directly by mixing two crude cell lysates, one cell lysate containing the plasmid and the other the protein affinity ligand, without the need for treatment by RNaseA. After IMAC chromatography, high purity supercoiled DNA is recovered in good yields of 100-150 μg plasmid per 200 mL shake flask culture. Moreover, the resulting DNA is free from linear or open-circular plasmid DNA, genomic DNA, RNA, and protein, to the limits of our detection. Furthermore, we show that lyophilized affinity ligand can be stored at room temperature and re-hydrated for use when required. © 2007 Wiley Periodicals, Inc.

Affinity purification of recombinant human plasminogen activator from transgenic rabbit milk using a novel polyolresponsive monoclonal antibody

Purpose: To develop processes for effective isolation and purification of recombinant human plasminogen activator (rhPA) from transgenic rabbit milk. Methods: Immunoaffinity chromatography was selected and improved by a special polyol-responsive monoclonal antibody (PR-mAb). Alteplase was used as immunogen because of its similarity to rhPA in terms of structure. The PR-mAb was prepared by hybridoma technology and screened by ELISA-elution assay. Screening antibody was performed using rhPA milk in an ELISA-elution assay. The antibody clone C4-PR-mAb was selected for immunoaffinity chromatography. The rhPA was effectively bound to immobilized C4-PR-mAb on the column and was eluted with Tris buffer comprising 0.75 mol/L ammonium sulfate and 40n% propanediol (pH7.9). The rhPA was further purified by passing through Chromdex75 gel filtration column. Results: There were 12 hybridoma strains selected into the polyol-responsive mAbs screen step and three hybridoma strains were superior for producing PR-mAbs (C1, C4, C8). The rhPA can be purified from transgenic rabbit milk and maintained a higher thrombolytic activity in vitro by FAPA. Conclusion: The results demonstrate the suitability of the alternative approach used in this study. Using immunoaffinity chromatography and gel filtration column is feasible and convenient for extracting rhPA from milk, and should be useful for purifying other tPA mutants or other novel recombinant milkderived proteins.

Paracoccin from Paracoccidioides brasiliensis; purification through affinity with chitin and identification of N-acetyl-beta-D-glucosaminidase activity

The dimorphic fungus Paracoccidioides brasiliensis is the causative agent of paracoccidioidomycosis, the most frequent systemic mycosis in Latin America. Our group has been working with paracoccin, a P. brasiliensis lectin with MM 70 kDa. which is purified by affinity, with immobilized N-acetylglucosamine (GlcNAc). Paracoccin has been described to play a role in fungal adhesion to extracellular matrix components and to induce high and persistent levels or TNF alpha. and nitric oxide production by macrophages. In the cell wall, paracoccin colocalizes with the beta-1,4-homopolymer of GlcNAc into the budding sites of the P. brasiliensis yeast cell. In this paper we present a protocol for the chitin-affinity purification or paracoccin. This procedure provided higher yields than those achieved by means of the technique based oil the affinity of this lectin with GlcNAc and had an impact on downstream assays. SDS-PAGE and Western blot analysis revealed similarities between the N-acetylglucosamine- and chitin-bound fractions, confirmed by MALDI-TOF-MS of trypsinic peptides. Western blot of two-dimensional gel electrophoresis of the yeast extract showed a major spot with M(r) 70000 and pl approximately 5.63. Moreover, an N-acetyl-beta-D-glucosaminidase activity was reported for paracoccin, thereby providing new insights into the mechanisms that lead to cell wall remodelling and opening new perspectives for its structural characterization. Copyright (C) 2009 John Wiley & Sons. Ltd.

Purification of recombinant proteins by chemical removal of the affinity tag.

The efficient removal of a N- or C-terminal purification tag from a fusion protein is necessary to obtain a protein in a pure and active form, ready for use in human or animal medicine. Current techniques based on enzymatic cleavage are expensive and result in the presence of additional amino acids at either end of the proteins, as well as contaminating proteases in the preparation. Here we evaluate an alternative method to the one-step affinity/protease purification process for large-scale purification. It is based upon the cyanogen bromide (CNBr) cleavage at a single methionine placed in between a histidine tag and a Plasmodium falciparum antigen. The C-terminal segment of the circumsporozoite polypeptide was expressed as a fusion protein with a histidine tag in Escherichia coli purified by Ni-NAT agarose column chromatography and subsequently cleaved by CNBr to obtain a polypeptide without any extraneous amino acids derived from the cleavage site or from the affinity purification tag. Thus, a recombinant protein is produced without the need for further purification, demonstrating that CNBr cleavage is a precise, efficient, and low-cost alternative to enzymatic digestion, and can be applied to large-scale preparations of recombinant proteins.

Purification par affinité et marquage isotopique spécifique pour études d’ARN fonctionnels

Il existe un lien étroit entre la structure tridimensionnelle et la fonction cellulaire de l’ARN. Il est donc essentiel d’effectuer des études structurales de molécules d’ARN telles que les riborégulateurs afin de mieux caractériser leurs mécanismes d’action. Une technique de choix, permettant d’obtenir de l’information structurale sur les molécules d’ARN est la spectroscopie RMN. Cette technique est toutefois limitée par deux difficultés majeures. Premièrement, la préparation d’une quantité d’ARN nécessaire à ce type d’étude est un processus long et ardu. Afin de résoudre ce problème, notre laboratoire a développé une technique rapide de purification des ARN par affinité, utilisant une étiquette ARiBo. La deuxième difficulté provient du grand recouvrement des signaux présents sur les spectres RMN de molécules d’ARN. Ce recouvrement est proportionnel à la taille de la molécule étudiée, rendant la détermination de structures d’ARN de plus de 15 kDa extrêmement complexe. La solution émergeante à ce problème est le marquage isotopique spécifique des ARN. Cependant, les protocoles élaborées jusqu’à maintenant sont très coûteux, requièrent plusieurs semaines de manipulation en laboratoire et procurent de faibles rendements. Ce mémoire présente une nouvelle stratégie de marquage isotopique spécifique d’ARN fonctionnels basée sur la purification par affinité ARiBo. Cette approche comprend la séparation et la purification de nucléotides marqués, une ligation enzymatique sur support solide, ainsi que la purification d’ARN par affinité sans restriction de séquence. La nouvelle stratégie développée permet un marquage isotopique rapide et efficace d’ARN fonctionnels et devrait faciliter la détermination de structures d’ARN de grandes tailles par spectroscopie RMN.

Adaptations de la méthode de purification d’ARN par affinité avec l’étiquette ARiBo

Dans les dernières années, une explosion de la recherche sur les ARN a eu lieue à cause de nombreuses découvertes démontrant l’importance de l’ARN dans plusieurs processus biologiques. Ainsi, de grandes quantités d’ARN sont devenues indispensables au bon déroulement de plusieurs études, notamment pour la biologie structurale et la caractérisation fonctionnelle. Cependant, il existe encore peu de méthodes de purification simples, efficaces, fiables et produisant un ARN sous forme native. Dans les dernières années, le laboratoire Legault a mis au point une méthode de purification par affinité utilisant une étiquette ARiBo pour la purification d’ARN transcrits in vitro par la polymérase à ARN du phage T7. Cette méthode de purification d’ARN a été spécifiquement développée pour maximiser la pureté et le rendement. De plus, elle est très rapide et fonctionne avec plusieurs types d’ARN. Cependant, comme plusieurs autres méthodes de purification, cette méthode produit des ARN avec des extrémités 5′ hétérogènes. Dans ce mémoire, des solutions sont proposées pour remédier au problème d’hétérogénéité en 5ʹ′ des ARN transcrits avec la polymérase à ARN du phage T7 et purifiés par la méthode ARiBo. La première solution consiste à choisir la séquence en 5′ parmi celles des 32 séquences testées qui ne présentent pas d’hétérogénéité en 5ʹ′. La seconde solution est d’utiliser une étiquette clivable en 5ʹ′ de l’ARN d’intérêt, tel que le ribozyme hammerhead, déjà utilisée pour ce genre d’application, ou le système CRISPR/Cse3 que nous proposons dans l’article présenté dans ce mémoire. De plus, nous avons adapté la méthode ARiBo pour rendre possible la purification d’un long ARN de 614 nt, le polycistron miR-106b-25. Nous avons également démontré la possibilité d’utiliser la méthode ARiBo pour l’isolation de protéines qui se lient à un ARN donné, le précurseur de miRNA pre-miR-153-2. En conclusion, ce mémoire démontre la possibilité d’adapter la méthode ARiBo à plusieurs applications.

SYNTHETIC OLIGODEOXYNUCLEOTIDE PURIFICATION VIA CATCHING BY POLYMERIZATION

Large quantities of pure synthetic oligodeoxynucleotides (ODNs) are important for preclinical research, drug development, and biological studies. These ODNs are synthesized on an automated synthesizer. It is inevitable that the crude ODN product contains failure sequences which are not easily removed because they have the same properties as the full length ODNs. Current ODN purification methods such as polyacrylamide gel electrophoresis (PAGE), reversed-phase high performance liquid chromatography (RP HPLC), anion exchange HPLC, and affinity purification can remove those impurities. However, they are not suitable for large scale purification due to the expensive aspects associated with instrumentation, solvent demand, and high labor costs. To solve these problems, two non-chromatographic ODN purification methods have been developed. In the first method, the full-length ODN was tagged with the phosphoramidite containing a methacrylamide group and a cleavable linker while the failure sequences were not. The full-length ODN was incorporated into a polymer through radical acrylamide polymerization whereas failure sequences and other impurities were removed by washing. Pure full-length ODN was obtained by cleaving it from the polymer. In the second method, the failure sequences were capped by a methacrylated phosphoramidite in each synthetic cycle. During purification, the failure sequences were separated from the full-length ODN by radical acrylamide polymerization. The full-length ODN was obtained via water extraction. For both methods, excellent purification yields were achieved and the purity of ODNs was very satisfactory. Thus, this new technology is expected to be beneficial for large scale ODN purification.

Purification of plasmid DNA for use in human gene therapy

Two key issues defined the focus of this research in manufacturing plasmid DNA for use In human gene therapy. First, the processing of E.coli bacterial cells to effect the separation of therapeutic plasmid DNA from cellular debris and adventitious material. Second, the affinity purification of the plasmid DNA in a Simple one-stage process. The need arises when considering the concerns that have been recently voiced by the FDA concerning the scalability and reproducibility of the current manufacturing processes in meeting the quality criteria of purity, potency, efficacy, and safety for a recombinant drug substance for use in humans. To develop a preliminary purification procedure, an EFD cross-flow micro-filtration module was assessed for its ability to effect the 20-fold concentration, 6-time diafiltration, and final clarification of the plasmid DNA from the subsequent cell lysate that is derived from a 1 liter E.coli bacterial cell culture. Historically, the employment of cross-flow filtration modules within procedures for harvesting cells from bacterial cultures have failed to reach the required standards dictated by existing continuous centrifuge technologies, frequently resulting in the rapid blinding of the membrane with bacterial cells that substantially reduces the permeate flux. By challenging the EFD module, containing six helical wound tubular membranes promoting centrifugal instabilities known as Dean vortices, with distilled water between the Dean number's of 187Dn and 818Dn,and the transmembrane pressures (TMP) of 0 to 5 psi. The data demonstrated that the fluid dynamics significantly influenced the permeation rate, displaying a maximum at 227Dn (312 Imh) and minimum at 818Dn (130 Imh) for a transmembrane pressure of 1 psi. Numerical studies indicated that the initial increase and subsequent decrease resulted from a competition between the centrifugal and viscous forces that create the Dean vortices. At Dean numbers between 187Dn and 227Dn , the forces combine constructively to increase the apparent strength and influence of the Dean vortices. However, as the Dean number in increases above 227 On the centrifugal force dominates the viscous forces, compressing the Dean vortices into the membrane walls and reducing their influence on the radial transmembrane pressure i.e. the permeate flux reduced. When investigating the action of the Dean vortices in controlling tile fouling rate of E.coli bacterial cells, it was demonstrated that the optimum cross-flow rate at which to effect the concentration of a bacterial cell culture was 579Dn and 3 psi TMP, processing in excess of 400 Imh for 20 minutes (i.e., concentrating a 1L culture to 50 ml in 10 minutes at an average of 450 Imh). The data demonstrated that there was a conflict between the Dean number at which the shear rate could control the cell fouling, and the Dean number at which tile optimum flux enhancement was found. Hence, the internal geometry of the EFD module was shown to sub-optimal for this application. At 579Dn and 3 psi TMP, the 6-fold diafiltration was shown to occupy 3.6 minutes of process time, processing at an average flux of 400 Imh. Again, at 579Dn and 3 psi TMP the clarification of the plasmid from tile resulting freeze-thaw cell lysate was achieved at 120 Iml1, passing 83% (2,5 mg) of the plasmid DNA (6,3 ng μ-1 10.8 mg of genomic DNA (∼23,00 Obp, 36 ng μ-1 ), and 7.2 mg of cellular proteins (5-100 kDa, 21.4 ngμ-1 ) into the post-EFD process stream. Hence the EFD module was shown to be effective, achieving the desired objectives in approximately 25 minutes. On the basis of its ability to intercalate into low molecular weight dsDNA present in dilute cell lysates, and be electrophoresed through agarose, the fluorophore PicoGreen was selected for the development of a suitable dsDNA assay. It was assesseel for its accuracy, and reliability, In determining the concentration and identity of DNA present in samples that were eleclrophoresed through agarose gels. The signal emitted by intercalated PicoGreen was shown to be constant and linear, and that the mobility of the PicaGreen-DNA complex was not affected by the intercalation. Concerning the secondary purification procedure, various anion-exchange membranes were assessed for their ability to capture plasmid DNA from the post-EFD process stream. For a commercially available Sartorius Sartobind Q15 membrane, the reduction in the equilibriumbinding capacity for  ctDNA in buffer of increasing ionic demonstrated that DNA was being.adsorbed by electrostatic  interactions only. However, the problems associated with fluid distribution across the membrane demonstrated that the membrane housing was the predominant cause of the .erratic breakthrough curves. Consequently, this would need to be rectified before such a membrane could be integrated into the current system, or indeed be scaled beyond laboratory scale. However, when challenged with the process material, the data showed that considerable quantities of protein (1150 μg) were adsorbed preferentially to the plasmid DNA (44 μg). This was also shown for derived Pall Gelman UltraBind US450 membranes that had been functionalised by varying molecular weight poly-L~lysine and polyethyleneimine ligands. Hence the anion-exchange membranes were shown to be ineffective in capturing plasmid DNA from the process stream. Finally, work was performed to integrate a sequence-specific DNA·binding protein into a single-stage DNA chromatography, isolating plasmid DNA from E.coli cells whilst minimising the contamination from genomic DNA and cellular protein. Preliminary work demonstrated that the fusion protein was capable of isolating pUC19 DNA into which the recognition sequence for the fusion-protein had been inserted (pTS DNA) when in the presence of the conditioned process material. Althougth the pTS recognition sequence differs from native pUC19 sequences by only 2 bp, the fusion protein was shown to act as a highly selective affinity ligand for pTS DNA alone. Subsequently, the scale of the process was scaled 25-fold and positioned directly following the EFD system. In conclusion, the integration of the EFD micro-filtration system and zinc-finger affinity purification technique resulted in the capture of approximately 1 mg of plasmid DNA was purified from 1L of E.coli  culture in a simple two stage process, resulting in the complete removal of genomic DNA and 96.7% of cellular protein in less than 1 hour of process time.

Membrane protein extraction and purification using styrene-maleic acid (SMA) co-polymer:effect of variations in polymer structure

The use of styrene maleic acid (SMA) co-polymers to extract and purify transmembrane proteins, whilst retaining their native bilayer environment, overcomes many of the disadvantages associated with conventional detergent based procedures. This approach has huge potential for the future of membrane protein structural and functional studies. In this investigation we have systematically tested a range of commercially available SMA polymers, varying in both the ratio of styrene to maleic acid and in total size, for the ability to extract, purify and stabilise transmembrane proteins. Three different membrane proteins (BmrA, LeuT and ZipA) which vary in size and shape were used. Our results show that several polymers can be used to extract membrane proteins comparably to conventional detergents. A styrene:maleic acid ratio of either 2:1 or 3:1, combined with a relatively small average molecular weight (7.5-10 kDa) is optimal for membrane extraction, and this appears to be independent of the protein size, shape or expression system. A subset of polymers were taken forward for purification, functional and stability tests. Following a one-step affinity purification SMA 2000 was found to be the best choice for yield, purity and function. However the other polymers offer subtle differences in size and sensitivity to divalent cations that may be useful for a variety of downstream applications.