Affinity adsorption of lysozyme on a macroligand prepared with Cibacron Blue 3GA attached to yeast cells

The objective of this study was the development of affinity adsorbent particles with the appropriate characteristics to be applied in protein purification using the affinity ultrafiltration method. To prepare affinity macroligands Cibacron Blue 3GA, as a ligand molecule, was immobilized by covalent bonding onto yeast cell walls, the support material or matrix. The maximum attachment of the ligand to the matrix was 212 μmol/g (ligand dry weight/yeast dry weight). Lysozyme was selected as the protein model for the adsorption studies. Its adsorption onto the matrix without ligand and matrix with attached ligand were investigated batch-wise. The adsorption equilibrium isotherms appeared to follow a typical Langmuir isotherm. The maximum adsorption capacity (q(m)) of the Cell-Cibacron macroligand for lysozyme was 110 mg/ml of wet macroligand. The adsorbent was also employed for the separation of lysozyme from hen egg white. High purity lysozyme was obtained.     

Use of the avidin (imino)biotin system as a general approach to affinity precipitation

Affinity precipitation, especially secondary effect affinity precipitation, has repeatedly been suggested as a valuable technique for the biotechnical downstream process. The present lack of applications is related to the scarcity of predictable affinity macroligands and to the fact that rather high affinity constants are required in affinity precipitation (K(D) < 10(-10)). The latter are rarely found in nature, at least in the case of small affinity ligands (affinity tags), and are usually difficult to handle (complex dissociation) once one has found them. In this article we describe a new type of thermoresponsive affinity macroligand. The base polymer (poly-N-isopropylacrylamide, or PNIPAAm) is produced by chain transfer polymerization. As a consequence, the structure, as well as the solubility behavior, is very homogeneous (polydispersity < 1.2), whereas the average molecular mass is small (<5000 g/mol). In pure water, the base polymer shows sharp thermoprecipitation at 32.2 degrees C. Each oligomer carries a single amino end group, which allows easy and defined coupling of the affinity ligand, while preserving the ligand's activity to the highest possible degree. Herein, the oligomer was coupled to iminobiotin. The ensuing affinity macroligand has a high affinity to avidin (and avidin-tagged molecules) at elevated pH (<10), but releases the avidin easily at lower pH (approximately 4). The affinity macroligands were used to purify avidin from solutions containing large amounts of lysozyme as well as from cell culture supernatants containing 5% fetal calf serum. In both cases, pure avidin was recovered (residual protein contamination below the detection limit), with yields of >90%.     

Challenges and opportunities in the purification of recombinant tagged proteins

The purification of recombinant proteins by affinity chromatography is one of the most efficient strategies due to the high recovery yields and purity achieved. However, this is dependent on the availability of specific affinity adsorbents for each particular target protein. The diversity of proteins to be purified augments the complexity and number of specific affinity adsorbents needed, and therefore generic platforms for the purification of recombinant proteins are appealing strategies. This justifies why genetically encoded affinity tags became so popular for recombinant protein purification, as these systems only require specific ligands for the capture of the fusion protein through a pre-defined affinity tag tail. There is a wide range of available affinity pairs “tag-ligand” combining biological or structural affinity ligands with the respective binding tags. This review gives a general overview of the well-established “tag-ligand” systems available for fusion protein purification and also explores current unconventional strategies under development.     

Affinity ultrafiltration: effects of ligand binding on selectivity and process optimization.

The effective design of affinity ultrafiltration processes using a selective macroligand requires a detailed understanding of the effects of ligand-binding interactions on product yield and purification. Theoretical calculations were performed to evaluate the performance of affinity diafiltration separations with both competitive and independent binding interactions for the product and impurity. The intrinsic selectivity for independent binding decreased during the diafiltration due to the increase in fractional impurity binding as the impurity is selectively removed. The opposite behavior was seen for competitive binding because the strongly bound product displaces the impurity from the binding sites. Purification-yield diagrams were used to examine the effects of affinity-ligand concentration and binding constants on the separation. Model calculations were in excellent agreement with experimental data for the separation of tryptophan isomers using bovine serum albumin as the steroselective macroligand. Simulations with a fixed number of diavolumes show a clear optimum in product yield and purification factor at an intermediate ligand concentration due to the competing effects of the intrinsic selectivity and the rate of impurity removal. These results provide an appropriate framework for the design and optimization of affinity ultrafiltration systems.     

Multistage affinity cross-flow filtration: process optimization

The recovery yield (REC) and productivity (PRD) are used as objective functions to optimize the multistage affinity cross-flow filtration (mACFF) process. The effects of the operating conditions such as feed loading volume (Q _L ⁺), total protein concentration and target protein purity in the feeding broth are analyzed. For higher affinity system or by a mACFF process with larger number of stages as well as more macroligand loading, there is a critical value of Q _L ⁺ below which the REC keeps constant and maximal. This maximal value of REC is affected by the stage number as well as macroligand loading of the mACFF process and the affinity system (i.e., the binding constant of the target protein to its macroligand), but independent of the feeding broth properties (i.e., total protein concentration and target protein purity) and membrane permeability. An optimum of Q _L ⁺ exists to give a maximum of PRD. The optimal Q _L ⁺ is somewhat larger than the critical Q _L ⁺ value below which REC keeps constant. The maximum of PRD is raised by increasing the stage number and macroligand loading of the mACFF process, affinity binding constant, and total protein concentration as well as target protein purity in the feeding broth, but reduced by increasing the membrane rejection coefficient (R). However, it is encouraging that the decrease of the maximal PRD is less significant when R is less than 0.5. Therefore, if it is not possible to find a membrane that is completely permeable to proteins and at the same time completely impermeable to the macroligand, a membrane with R less than 0.5 may be selected to obtain a larger PRD. The results obtained in this work give further predictive understanding of the mACFF technique, and will be useful to the process design.     

Purification of histidine-tagged single-chain Fv-antibody fragments by metal chelate affinity precipitation using thermoresponsive copolymers

Metal chelate affinity precipitation (MCAP) has been successfully developed as a simple purification process for proteins that have affinity for metal ions. The present lack of widespread applications for this technique as compared to immobilized metal affinity chromatography (IMAC) may be related to the scarcity of well-characterized metal affinity macroligands (AML) and their applications to the number of different purification systems. In the present work we describe a detailed study of a new purification system using metal-loaded thermoresponsive copolymers as AML. The copolymers of vinylimidazole (VI) with N-isopropylacrylamide (NIPAM) were synthesized by radical polymerization with imidazole contents of 15 and 24 mol%. When loaded with Cu(II) and Ni(II) ions the copolymers selectively precipitated extracellularly expressed histidine-tagged single-chain Fv-antibody fragments (His(6)-scFv fragments) from the fermentation broth free from E. coli cells. Precipitation was induced by salt at mild temperatures and the bound antibody fragments were recovered by dissolving the protein-polymer complex in EDTA buffer and subsequent reprecipitation of the polymer. His(6)-scFv fragments were purified with yields of 91 and 80% and purification folds of 16 and 21 when Cu(II) and Ni(II) copolymers were used, respectively. The protein precipitation capacity of the Ni(II) copolymer showed a dependence on the VI concentration in the copolymer. The SDS-PAGE pattern showed significant purification of the antibody fragments.     

Recombinant enterokinase light chain with affinity tag: expression from Saccharomyces cerevisiae and its utilities in fusion protein technology.

Enterokinase and recombinant enterokinase light chain (rEK(L)) have been used widely to cleave fusion proteins with the target sequence of (Asp)(4)-Lys. In this work, we show that their utility as a site-specific cleavage agent is compromised by sporadic cleavage at other sites, albeit at low levels. Further degradation of the fusion protein in cleavage reaction is due to an intrinsic broad specificity of the enzyme rather than to the presence of contaminating proteases. To offer facilitated purification from fermentation broth and efficient removal of rEK(L) after cleavage reaction, thus minimizing unwanted cleavage of target protein, histidine affinity tag was introduced into rEK(L). Utilizing the secretion enhancer peptide derived from the human interleukin 1 beta, the recombinant EK(L) was expressed in Saccharomyces cerevisiae and efficiently secreted into culture medium. The C-terminal His-tagged EK(L) was purified in a single-step procedure on nickel affinity chromatography. It retained full enzymatic activity similar to that of EK(L), whereas the N-terminal His-tagged EK(L) was neither efficiently purified nor had any enzymatic activity. After cleavage reaction of fusion protein, the C-terminal His-tagged EK(L) was efficiently removed from the reaction mixture by a single passage through nickel-NTA spin column. The simple affinity tag renders rEK(L) extremely useful for purification, post-cleavage removal, recovery, and recycling and will broaden the utility and the versatility of the enterokinase for the production of recombinant proteins.     

Engineering a high-affinity scaffold for non-chromatographic protein purification via intein-mediated cleavage

While protein purification has long been dominated by standard chromatography, the relatively high cost and complex scale‐up have promoted the development of alternative non‐chromatographic separation methods. Here we developed a new non‐chromatographic affinity method for the purification of proteins expressed in Escherichia coli. The approach is to genetically fuse the target proteins with an affinity tag. Direct purification and recovery can be achieved using a thermo‐responsive elastin‐like protein (ELP) scaffold containing the capturing domain. Naturally occurring cohesin–dockerin pairs, which are high‐affinity protein complex responsible for the formation of cellulosome in anaerobic bacteria, were used as the model. By exploiting the highly specific interaction between the dockerin and cohesin domain from Clostridium thermocellum and the reversible aggregation property of ELP, highly purified and active dockerin‐tagged proteins, such as the endoglucanase CelA, chloramphenicol acetyl transferase (CAT), and enhanced green fluorescence protein (EGFP), were recovered directly from crude cell extracts in a single thermal precipitation step with yields achieving over 90%. Incorporation of a self‐cleaving intein domain enabled rapid removal of the affinity tag from the target proteins, which was subsequently removed by another cycle of thermal precipitation. This method offers great flexibility as a wide range of affinity tags and ligands can be used. Biotechnol. Bioeng. 2012; 109: 2829–2835. © 2012 Wiley Periodicals, Inc.     

Purification of NSP1 reveals complex formation with 'GLFG' nucleoporins and a novel nuclear pore protein NIC96.

The essential C-terminal domain of NSP1 mediates assembly into the nuclear pore complex (NPC). To identify components which interact physically with this yeast nucleoporin, the tagged C-terminal domain of NSP1 (ProtA-NSP1) was isolated by affinity chromatography under non-denaturing conditions. The purified complex contains ProtA-NSP1, two previously identified 'GLFG' nucleoporins, NUP49 (NSP49) and p54 and a novel protein designated NIC96 (for Nucleoporin-Interacting Component of 96 kDa). Conversely, affinity purification of tagged NSP49 enriches for NSP1, the p54 and the NIC96 component. The NIC96 gene was cloned; it encodes a novel 839 amino acid protein essential for cell growth. By immunofluorescence, protein A-tagged NIC96 exhibits a punctate nuclear membrane staining indicative of nuclear pore location. Therefore, affinity purification of tagged nucleoporins has allowed the definition of a subcomplex of the NPC and analysis of physical interactions between nuclear pore proteins.     

Sterol Composition in the Pollens of Citrus unshiu Marcov. and Citrus sinensis Osbeck

Bacillus brevis secretes a large amount of cell wall proteins into the culture medium. For construction of Bacillus brevis expression-secretion vectors of human erythropoietin (EPO) and the extracellular domain of mouse erythropoietin receptor (sEPOR), cDNA for each mature form was inserted into a plasmid containing the promoter region and the signal-peptide encoding region of a cell wall protein. Culture supernatants of transformants were affinity purified using a monoclonal antibody-fixed gel for EPO and an EPO-fixed gel for sEPOR. The affinity purification efficiently removed unwanted proteins, giving samples with sufficiently high purity to analyze amino acid sequences of N-terminal regions and biological activities. Combination of this secretory production and affinity purification may facilitate isolation of a large amount of pure EPO and sEPOR, and is useful for further understanding the molecular mechanism of interaction between EPO and EPOR.     

Separation methods in the analysis of protein membrane complexes

The separation of membrane protein complexes can be divided into two categories. One category, which is operated on a relatively large scale, aims to purify the membrane protein complex from membrane fractions while retaining its native form, mainly to characterize its nature. The other category aims to analyze the constituents of the membrane protein complex, usually on a small scale. Both of these face the difficulty of isolating the membrane protein complex without interference originating from the hydrophobic nature of membrane proteins or from the close association with membrane lipids. To overcome this difficulty, many methods have been employed. Crystallized membrane protein complexes are the most successful example of the former category. In these purification methods, special efforts are made in the steps prior to the column chromatography to enrich the target membrane protein complexes. Although there are specific aspects for each complex, the most popular method for isolating these membrane protein complexes is anion-exchange column chromatography, especially using weak anion-exchange columns. Another remarkable trend is metal affinity column chromatography, which purifies the membrane protein complex as an intact complex in one step. Such protein complexes contain subunit proteins which are genetically engineered so as to include multiple-histidine tags at carboxyl- or amino-termini. The key to these successes for multi-subunit complex isolation is the idea of keeping the expression at its physiological level, rather than overexpression. On the other hand, affinity purification using the Fv fragment, in which a Strep tag is genetically introduced, is ideal because this method does not introduce any change to the target protein. These purification methods supported by affinity interaction can be applied to minor membrane protein complexes in the membrane system. Isoelectric focusing (IEF) and blue native (BN) electrophoresis have also been employed to prepare membrane protein complexes. Generally, a combination of two or more chromatographic and/or electrophoretic methods is conducted to separate membrane protein complexes. IEF or BN electrophoresis followed by 2nd dimension electrophoresis serve as useful tools for analytical demand. However, some problems still exist in the 2D electrophoresis using IEF. To resolve such problems, many attempts have been made, e.g. introduction of new chaotropes, surfactants, reductants or supporting matrices. This review will focus in particular on two topics: the preparative methods that achieved purification of membrane protein complexes in the native (intact) form, and the analytical methods oriented to resolve the membrane proteins. The characteristics of these purification and analytical methods will be discussed along with plausible future developments taking into account the nature of membrane protein complexes.     

The Bead blot: a method for identifying ligand-protein and protein-protein interactions using combinatorial libraries of peptide ligands

Small molecules that bind proteins can be used as ligands for protein purification and for investigating protein-protein and protein-drug interactions. Unfortunately, many methods used to identify new ligands to desired proteins suffer from common shortcomings, including the requirement that the target protein be purified and/or the requirement that the ligands be selected under conditions different from those under which it will be used. We have developed a new method called the Bead blot that can (i) select ligands to unpurified proteins, including trace proteins, present in complex materials (e.g., unfractionated plasma); (ii) select ligands to multiple proteins under a variety of conditions in a single experiment; and (iii) be used with libraries of different types of ligands. In the Bead blot, a library of ligands, synthesized on chromatography resin beads, is incubated with a starting material containing a target protein for which a ligand is sought. The proteins in the material bind to their complementary ligands according to specific affinity interactions. Then the protein-loaded beads are immobilized in a porous matrix, and the proteins are directionally eluted from the beads and captured on a membrane superimposed on the beads. The location of the target protein on the membrane is determined, and because the position of the protein(s) on the membrane reflects the position of the bead(s) in the matrix, the bead that originally bound the protein is identified, with subsequent elucidation of the ligand sequence. Ligands to several targets can be identified in one experiment. Here we demonstrate the broad utility of this method by the selection of ligands that purify plasma protein complexes or that remove pathogens from whole blood with very high affinity constants. We also select ligands to a protein based on competitive elution.     

Essential role of the concentration of immobilized ligands in affinity chromatography:: Purification of guanidinobenzoatase on an ionized ligand

Guanidinobenzoatase, a plasma protein with possible application as a ‘tumor marker’, has been fully purified by one-step affinity chromatography. The affinity matrix was prepared by ‘controlled’ immobilization of an enzyme inhibitor (agmatine) onto commercial agarose gels containing carboxyl moieties activated as N-hydroxysuccinimide esters. In this way, agmatine becomes immobilized through an amido bond and preserves an ionized guanidino moiety. Different matrices with different concentration of ligands were prepared in order to evaluate their properties as affinity supports. Interestingly, matrices with a very low concentration of immobilized ligands (2 μmol/ml, corresponding to the modification of only 5% of active groups in the commercial resins) exhibited a low capacity for unspecific adsorption of proteins (as anion-exchange resins) and displayed also a high capacity for specific adsorption of our target protein. On the other hand, when affinity matrices possessed a moderate concentration of agmatine (10 μmol/ml of gel or higher), two undesirable phenomena were observed: (a) the matrix behaves as a very good anionic exchange support able to non-specifically adsorb most of plasma proteins and (b) the specific adsorption of our target protein becomes much lower. The latter phenomenon could be due to steric hindrances promoted by the interaction between each individual immobilized ligand and the corresponding binding pocket in the target protein. These hindrances could also be promoted by the presence of a fairly dense layer of immobilized ligands covering the support surface, thus preventing interactions between immobilized ligands and partially buried protein-binding pockets. In this way, a successful affinity purification (23.5% yield, ×220 purification factor, a unique electrophoretic band) could be achieved by combination of three approaches: (i) the use of affinity matrices possessing a very low density of immobilized ligands, (ii) performing affinity adsorption at high ionic strength and (iii) performing specific desorption with substrates or substrate analogues.     

Challenges and recent advances in affinity purification of tag-free proteins

There is currently no generic, simple, low-cost method for affinity chromatographic purification of proteins in which the purified product is free of appended tags. Existing approaches for the purification of tagless proteins fall into two broad categories: (1) direct affinity-based capture of tag-free proteins that utilize affinity ligands specific to the target protein or class of target protein, and (2) removal of an appended affinity tag following tag-mediated protein capture. This paper reviews current state-of-the-art approaches for tagless protein purification in both categories, including specific examples of affinity ligands used for the capture of different classes of proteins and cleavage systems for affinity tag removal following chromatographic capture. A particular focus of this review is on recent developments in affinity tag removal systems utilizing split inteins.     

A continuous affinity ultrafiltration process for trypsin purification

A continuous process has been devised and tested for purification of a crude trypsin preparation from pig pancreas. The development was based on the principles of affinity chromatography and Ultrafiltration. Trypsin was selectively attracted by a water-soluble high molecular weight (>100,000) polymer, bearing a potent and specific trypsin inhibitor, m-aminobenzamidine. The trypsin-macroligand complex was then retained by using an appropriate Ultrafiltration membrane, while impurities could pass through. The bound trypsin was eluted by either arginine or benzamidine. The process also featured provision for recirculation of the eluant as well as the macroligand. It was demonstrated that this purification process could purify trypsin from the crude preparation with a yield of 77%, contaminated with only 3% of impurities. For the first time, a serious attempt has been made toward continuous purification of enzymes by the affinity Ultrafiltration technique. Besides a substantial increase in productivity, the affinity polymer could be easily reconditioned and expected to possess a long operative life. Such characteristics undoubtedly will play an important role in reducing the cost of trypsin purification.     

The Bead blot: a method for selecting small molecule ligands for protein capture and purification

We present a new method for selecting peptide ligands that are useful for protein purification, protein targeting and exploring protein-ligand interactions, and which requires no prior protein purification or derivatization. In the Bead blot, a complex mixture containing the target protein, for example, plasma, is incubated with a combinatorial library of peptide ligands synthesized on beads. The proteins are fractionated and purified on their respective ligands and the beads with their bound proteins are immobilized in a gel. The proteins are eluted from the ligands by capillary action and captured on a membrane so that their position on the membrane corresponds to the position of the beads in the gel. The protein is detected on the membrane, generating spots on an autoradiography film, the spots on the film are aligned with the beads in the gel, and the beads that bound the protein are recovered. The ligand on the bead(s) can be sequenced and synthesized at large scale for protein purification. The Bead blot can be completed in several hours with overnight pause steps if desired. On average, 5 prospective ligands are selected per 50,000 beads screened using this method. Unlike other ligand identification methods, the target protein does not have to be purified or labeled, and the Bead blot allows ligands for multiple proteins to be selected in a single experiment.     

The purification of recombinant hepatitis B surface antigen by hollow fibre ultrafiltration membrane diafiltration

Summary Recombinant hepatitis B surface antigen (HBsAg) broth was purified by diafiltration with a hollow fibre ultrafiltration membrane (cut off 100 kDa), by pre—treating the HBsAg broth with enzyme, most of the contaminating proteins was removed and very high recovery ratio of HBsAg was achieved. When HBsAg solution was concentrated using hollow fibre ultrafiltration membrane to 10% of its original volume, the HBsAg was recovered almost completely. Accordingly, membrane purification of HBsAg is a high yield, fast method.     

Membrane technology for purification of therapeutic proteins

Membrane systems are used throughout the downstream purification in the commercial production of high value therapeutic proteins. Over the last two decades, new membranes, modules, and systems have been developed specifically to meet the requirements of the biotechnology industry. These developments have been facilitated by an improved fundamental understanding of: (1) the effects of electrostatic interactions and concentration polarization on protein transmission during ultrafiltration and (2) the role of membrane morphology on protein fouling during both sterile and virus filtration. This perspective highlights some of the key work in this area and provides insights into possible future improvements in membrane technology for the purification of recombinant therapeutic proteins. Biotechnol. Bioeng. 2009;103: 227–230. © 2009 Wiley Periodicals, Inc.     

Purification of a membrane glycoprotein with an inositol-containing phospholipid anchor from Dictyostelium discoideum.

Large-scale purification of a Dictyostelium discoideum cell surface glycoprotein, which is anchored in the membrane via a glycosylphosphatidylinositol (GPI) moiety, is described. The purification protocol involved four steps: separation of crude cell membranes by low-speed centrifugation, delipidization of these membranes using acetone, extraction of the membrane proteins using the detergent Octyl beta-D-thioglucopyranoside (OTP), and purification of a specific membrane protein by monoclonal antibody immunoaffinity chromatography. The protein purified, PsA (prespore-specific antigen), is a developmentally regulated membrane glycoprotein found on a subset of cells from the cellular slime mould, D. discoideum. The protocol provides an efficient, economical, and technically simple way to purify GPI proteins in sufficient quantities for structural and functional studies. PsA was recovered at a yield of about 60%; with a purity of 97%, the extraction of 1 x 10(10) cells (1.1 g dry weight) yielded about 0.5 mg PsA glycoprotein. Techniques are described for growing kilogram quantities of D. discoideum cells in stainless steel trays at little cost. D. discoideum has considerable potential as a novel expression system for the production of foreign membrane-associated proteins. The purification strategy provides a means of purifying other GPI proteins, including those produced by protein engineering techniques.     

Purification of recombinant BtpA and Ycf3, proteins involved in membrane protein biogenesis in Synechocystis PCC 6803

The gene products Ycf3 (hypothetical chloroplast open reading frame) and BtpA (biogenesis of thylakoid protein) are thought to be involved in the biogenesis of the membrane protein complex photosystem I (PSI) from Synechocystis PCC 6803. PSI consists of 12 different subunits and binds more than 100 cofactors, making it a model protein to study different aspects of membrane protein biogenesis. For a detailed biophysical characterization of Ycf3 and BtpA pure proteins must be available in sufficient quantities. Therefore we cloned the corresponding genes into expression vectors. To facilitate purification we created His-tagged versions of Ycf3 and BtpA in addition to the unmodified forms. Immobilized metal affinity chromatography (IMAC) yielded His-tagged proteins which were used for the production of antibodies. Purification strategies for non-tagged proteins could also be established: Ycf3 could be purified in soluble form using a two-step purification in which ammonium sulfate precipitation was combined with anion-exchange chromatography (IEC). BtpA had to be purified from inclusion bodies by two-consecutive IEC steps under denaturing conditions. An optimized refolding protocol was established that yielded pure BtpA. In all cases, MALDI-TOF peptide mass fingerprinting (PMF) was used to confirm protein identity. Initially, size exclusion chromatography and CD-spectroscopy were used for biophysical characterization of the proteins. Both Ycf3 and BtpA show homo-oligomerization in vitro. In summary, purification protocols for Ycf3 and BtpA have been designed that yield pure proteins which can be used to probe the molecular function of these proteins for membrane protein biogenesis.