High-level synthesis in Escherichia coli of functional cap-binding eukaryotic initiation factor eIF-4E and affinity purification using a simplified cap-analog resin

Numerous studies have established the important role that eukaryotic initiation factor-4E (eIF-4E) plays during protein biosynthesis. However, biochemical characterization of eIF-4E has proved difficult, mainly because of its low abundance in cells. To facilitate studies on eIF-4E, we have overexpressed Saccharomyces cerevisiae eIF-4E in Escherichia coli. The isolation of eIF-4E was simplified by using a cap-analog affinity matrix (agarose resin) that is considerably less demanding to prepare than those previously reported. We describe a simple and rapid purification scheme that can yield 2-5 micrograms of a homogenous and active preparation of eIF-4E from 1 ml of E. coli culture. E. coli-expressed eIF-4E is active as determined by its ability to bind the cap structure. The results demonstrate that the cap-binding activity of eIF-4E is not dependent on the presence of other proteins that are present at low levels in eIF-4E preparations isolated from eukaryotic cells.     

Two-stage affinity purification for inducibly phosphorylated membrane proteins

Characterisation of tyrosine phosphorylations induced in immune cells in response to inflammatory stimuli may help elucidate the molecular bases of the diversity of immune responses. We have used anti-phosphotyrosine antibodies in combination with cell surface biotinylation in a two-step affinity purification procedure to recover pervanadate-induced tyrosine phosphorylated proteins from sub-cellular compartments, including the cell surface, of murine T cells and macrophages prior to separation by solution-phase isoelectric focussing and one-dimensional gel electrophoresis and identification by tandem mass spectrometry.     

Inteins and affinity resin substitutes for protein purification and scale up

The development of self-cleaving fusion-tag technology has greatly simplified the purification of recombinant proteins at laboratory scale. The self-cleaving capability of these tags has recently been combined with additional purification tags to generate novel and convenient protein purification methods at a variety of scales. In this review, we describe some of these methods, and provide a rudimentary economic analysis of hypothetical large-scale applications. This work is expected to provide a rough outline for the evaluation of these methods for large-scale bioprocessing of a variety of products.     

Small molecule-based chemical affinity system for the purification of proteins

A new chemical affinity system is described for the purification of proteins. The Linx Affinity Purification System enables researchers to quickly and easily bind a protein ligand to a chromatographic matrix and use the resulting affinity resin to purify a second protein from crude mixtures. The entire process takes approximately 2 h.     

Development of a novel affinity chromatography resin for platform purification of lambda fabs

Antigen‐binding fragments (Fabs) are novel formats in the growing pipeline of biotherapeutics. Sharing similar features to monoclonal antibodies (mAbs) with regard to expression, Fabs are considered as unchallenging for upstream development. Yet for downstream processing, the mature mAb downstream purification platform is not directly applicable. New approaches need to be found to achieve a lean purification process that maintains quality, productivity, and timelines while being generically applicable independent of the expression system. In a successful collaboration, BAC BV, GE Healthcare, and Novartis Pharma AG have developed a new affinity chromatography medium (resin) suitable to support cGMP manufacturing of lambda Fabs. We show that using this novel chromatography medium for the capture step, a purification platform for lambda Fabs can be established. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:1311–1318, 2014     

A parallel affinity purification method for selective isolation of polyubiquitinated proteins

We developed a parallel affinity purification (PAP) procedure, in which ubiquitinated proteins are purified from the cells that coexpress two affinity-tagged ubiquitins by sequential use of affinity chromatography specific to each tag. In contrast with previous procedures using a single affinity-tagged ubiquitin, the PAP eliminates highly abundant ubiquitin monomers and monoubiquitinated proteins to selectively enrich proteins bearing both affinity-tags, or poly- and multiubiquitinated proteins. Accordingly, it would serve as a powerful method to facilitate mass-spectrometric identification of ubiquitinated proteins.     

Chitosan/cellulose-based beads for the affinity purification of histidine-tagged proteins

Chitosan/cellulose-based beads (CCBs) for the affinity purification of histidine-tagged proteins were prepared from chitosan/cellulose dissolved in ionic liquid as a solvent, and their structures were characterized by Fourier transform infrared spectroscopy, transmission electron microscopy, and thermogravimetric analysis. The affinity purification was used to separate hexahistidine-tagged (his-tagged) enhanced green fluorescent protein (EGFP) from Escherichia coli. The results showed that Zn²⁺–CCB exhibited more specific adsorption capacity toward the target protein compared with Ni²⁺–CCB and Cu²⁺–CCB. The maximum adsorption of EGFP was 1.84?mg/g of Zn²⁺–CCB, with 90% purity under the optimized conditions (ionic strength (1.0?M NaCl), pH (7.2) and imidazole concentration (500?mM)). In addition, a regeneration method for the sorbent was further developed by washing with ethylenediaminetetraacetic acid disodium and then reimmobilizing with metal ions. This technique is an alternative method for the purification of his-tagged proteins, making the process more economical, fast, stable, and large batch.     

Review of conformation-specific affinity purification methods for plasma vitamin K-dependent proteins

There are seven known vitamin K-dependent proteins in blood. These proteins require calcium ion for expressing their full biological activities. Calcium ion also induces conformational changes in this class of proteins. Taking advantage of the ligand induced conformational changes, a number of unique approaches of affinity chromatography have been developed. These methodologies have been very useful tools for both the purification and for understanding the structure–function relationships of this class of proteins. One method is the use of metal ion dependent immunoaffinity chromatography. The antigen can be dissociated from the antibodies with either the removal or addition of calcium ion under physiological conditions. The other method is pseudoaffinity chromatography. This method uses conventional ion-exchange or hydrophobic resin and manipulates the mobilities of the proteins on these resins by the presence or absence of calcium ions. Researchers working with other calcium binding proteins or other proteins that are known to undergo ligand induced conformational changes may benefit from the experience of these unique conformation-specific affinity chromatography approaches.     

Optimization of affinity and ion-exchange chromatographic processes for the purification of proteins

This study documents several alternative approaches for the optimization of the ion-exchange and affinity chromatographic purification of proteins. In these approaches, the chromatographic process has been treated as a four-stage (adsorption, washing, elution, and regeneration) operation. Central to these investigations has been the elaboration of practical iterative procedures based on the use of theoretical models describing each of these stages. Predictions derived from these models have then been evaluated in terms of experimental data obtained using batch adsorption measurements in finite bath configurations and frontal breakthrough measurements with packed beds of different dimensions, containing nonporous and porous adsorbents of different selectivities and capacities for proteins. Commencing with the kinetic and distribution parameters derived from batch equilibrium measurements, the effect of the initial concentration of the target protein, the solid-liquid volume ratio, the superficial velocity and the column dimensions on the pressure drop, production rate, concentration profile, column utilization, and yield have been determined with packed beds. The potential of these iterative approaches to simplify the determination of key mass transfer and interaction parameters required for scale-up and economic optimization of chromatographic purifications of proteins has been examined using ion exchange, immobilized metal ion affinity, and triazine dye pseudo-affinity adsorbents of different selectivity and adsorption capacities. (c) 1996 John Wiley & Sons, Inc.     

Novel purification system for 6xHis-tagged proteins by magnetic affinity separation

We have developed a novel nickel-silica matrix for the generation of magnetic beads for metal-ion affinity chromatography. In contrast to magnetic Ni-NTA agarose beads, the novel particle type (SiMAC) consists of a magnetic core and a nickel-silica composite matrix with the nickel ions tightly integrated in the silica. This results in a much higher number of chelating groups compared with Ni-NTA agarose beads. With the SiMAC beads, greatly improved purification of histidine-tagged proteins from crude bacterial extracts was achieved. The yield was at least twice as high as with conventional materials, the method is faster, since the coupling step is omitted and there is no need for handling toxic Ni(2+) salts.     

Expression and affinity purification of recombinant proteins from plants

With recent advances in plant biotechnology, transgenic plants have been targeted as an inexpensive means for the mass production of proteins for biopharmaceutical and industrial uses. However, the current plant purification techniques lack a generally applicable, economic, large-scale strategy. In this study, we demonstrate the purification of a model protein, beta-glucuronidase (GUS), by employing the protein calmodulin (CaM) as an affinity tag. In the proposed system, CaM is fused to GUS. In the presence of calcium, the calmodulin fusion protein binds specifically to a phenothiazine-modified surface of an affinity column. When calcium is removed with a complexing agent, e.g., EDTA, calmodulin undergoes a conformational change allowing the dissociation of the calmodulin-phenothiazine complex and, therefore, permitting the elution of the GUS-CaM fusion protein. The advantages of this approach are the fast, efficient, and economical isolation of the target protein under mild elution conditions, thus preserving the activity of the target protein. Two types of transformation methods were used in this study, namely, the Agrobacterium-mediated system and the viral-vector-mediated transformation system.     

New matrices for the purification of pectinases by affinity chromatography

Polygalacturonic acid was used as a ligand in the affinity technique for pectinases purification from the filtrate of Aspergillus niger 71 culture. For this purpose four matrices were examined, namely, alkylamine controlled porous glass (CPG), alkylamine silica gel as well as keratin or polyamide coated silica gel. Good results of pectinase purification was obtained on silanized CPG or keratin coated silica gel supports.     

Observations on different resin strategies for affinity purification mass spectrometry of a tagged protein

Co-affinity purification mass spectrometry (CoAP-MS) is a highly effective method for identifying protein complexes from a biological sample and inferring important interactions, but the impact of the solid support is usually not considered in design of such experiments. Affinity purification (AP) experiments typically utilize a bait protein expressing a peptide tag such as FLAG, c-Myc, HA or V5 and high affinity antibodies to these peptide sequences to facilitate isolation of a bait protein to co-purify interacting proteins. We observed significant variability for isolation of tagged bait proteins between Protein A/G Agarose, Protein G Dynabeads, and AminoLink resins. While previous research identified the importance of tag sequence and their location, crosslinking procedures, reagents, dilution, and detergent concentrations, the effect of the resin itself has not been considered. Our data suggest the type of solid support is important and, under the conditions of our experiments, AminoLink resin provided a more robust solid-support platform for AP-MS.     

Single-process expression and purification of multiple recombinant proteins through cocultivation and affinity purification

Multiple recombinant proteins can be expressed simultaneously by inoculating multiple seed cultures into a single growth medium and inducing protein expression at a single time point. Up to three recombinant proteins can be individually purified from such a mixed culture (cocultivation) through the use of a combination of a multihistidine and a modified intein as affinity tags and the Ni sepharose and chitin as affinity matrices. This method may facilitate the study of protein complexes by rapidly obtaining multiple protein components in a single process and may potentially increase the efficiency of recombinant protein production at research and industrial scales.     

A dual protease approach for expression and affinity purification of recombinant proteins

We describe a new method for affinity purification of recombinant proteins using a dual protease protocol. Escherichia coli maltose binding protein (MBP) is employed as an N-terminal tag to increase the yield and solubility of its fusion partners. The MBP moiety is then removed by rhinovirus 3C protease, prior to purification, to yield an N-terminally His₆-tagged protein. Proteins that are only temporarily rendered soluble by fusing them to MBP are readily identified at this stage because they will precipitate after the MBP tag is removed by 3C protease. The remaining soluble His₆-tagged protein, if any, is subsequently purified by immobilized metal affinity chromatography (IMAC). Finally, the N-terminal His₆ tag is removed by His₆-tagged tobacco etch virus (TEV) protease to yield the native recombinant protein, and the His₆-tagged contaminants are removed by adsorption during a second round of IMAC, leaving only the untagged recombinant protein in the column effluent. The generic strategy described here saves time and effort by removing insoluble aggregates at an early stage in the process while also reducing the tendency of MBP to “stick” to its fusion partners during affinity purification.     

Fractionation of whey proteins with a hexapeptide ligand affinity resin

The isolation of individual proteins from whey would allow production of more consistent and reliable products by the food industry and possibly would also increase their use in the pharmaceutical industry. -Lactalbumin is the second most prevalent protein in bovine milk whey and has many uses including serving as an excellent protein source in infant formulas, power drinks and other beverages that require soluble, nutritional protein. In this study, we describe two methods for production of -lactalbumin from whey protein isolate using bioselective adsorption. The use of a peptide ligand (WHWRKR) attached to a resin allowed production of an -lactalbumin-rich fraction with a purity of 90.6% and a recovery of 47.9%, while also producing other fractions of commercial interest. The combined use of an amino resin followed by the WHWRKR resin produce a highly purified -lactalbumin (100%) with a yield of 35.2%.     

Rapid purification of mammalian 70,000-dalton stress proteins: affinity of the proteins for nucleotides.

A new and rapid purification procedure has been developed for the mammalian 70,000-dalton (70-kDa) heat-shock (or stress) proteins. Both the constitutive 73-kDa protein and the stress-induced 72-kDa protein have been purified by a two-step procedure employing DE52 ion-exchange chromatography followed by affinity chromatography on ATP-agarose. The two proteins, present in approximately equal amounts in either the 12,000 X g supernatant or pellet of hypotonically lysed heat-shock-treated HeLa cells, were found to copurify in relatively homogenous form. The purified proteins were covalently labeled with the fluorescent dye tetramethylrhodamine isothiocyanate, and the fluorescently labeled proteins were introduced back into living rat embryo fibroblasts via microinjection. The microinjected cells maintained at 37 degrees C showed only diffuse nuclear and cytoplasmic fluorescence. After heat-shock treatment of the cells, fluorescence was observed throughout the nucleus and more prominently within the nucleolus. This result is consistent with our earlier indirect immunofluorescence studies which showed a nuclear and nucleolar distribution of the endogenous 72-kDa stress protein in heat-shock-treated mammalian cells. The result also indicates that, for at least the 72-kDa protein, (i) the protein has been purified in apparently "native" form and (ii) its nucleolar distribution is stress dependent.     

Clathrin assembly proteins: affinity purification and a model for coat assembly

Assembly protein (AP) preparations from bovine brain coated vesicles have been fractionated by clathrin-Sepharose affinity chromatography. Two distinct fractions that possess coat assembly activity were obtained and are termed AP-1 and AP-2. The AP-1, not retained on the resin, has principal components with molecular weights of 108,000, 100,000, 47,000, and 19,000. The AP-2, bound to the resin and eluted by Tris-HCl at a concentration that parallels the latter's effect on coat disassembly, corresponds to the active complex described previously (Zaremba, S., and J. H. Keen, 1983, J. Cell Biol., 97:1339-1347). Its composition is similar to that of the AP-1 in that it contains 100,000-, 50,000-, and 16,000-mol-wt polypeptides in equimolar amounts; minor amounts of 112,000- and 115,000-mol-wt polypeptides are also present. Both are distinct from a recently described assembly protein of larger subunit molecular weight that we term AP-3. These results indicate the existence of a family of assembly proteins within cells. On incubation with clathrin both AP-1 and AP-2 induce the formation of coat structures, those containing AP-1 slightly smaller (mean diameter = 72 nm) than those formed in the presence of AP-2 (mean diameter = 79 nm); both structures have been detected previously in coated vesicle preparations from brain. Coats formed in the presence of AP-2 consistently contain approximately one molecule each of the 100,000-, 50,000-, and 16,000-mol-wt polypeptides per clathrin trimer. By low angle laser light scattering the molecular weight of native AP-2 was determined to be approximately 343,000, indicating that it is a dimer of each of the three subunits, and implying that it is functionally bivalent in clathrin binding. A model for AP-mediated coat assembly is proposed in which a bivalent AP-2 molecule bridges the distal legs or terminal domains of two clathrin trimers that are destined to occupy adjacent vertices in the assembled coat. Binding of a second AP-2 molecule locks these two trimers in register for assembly and further addition of AP-2 to free trimer legs promotes completion of the clathrin lattice. Effects of AP binding on the angle and flexibility of the legs at the hub of the trimer (the "pucker") are suggested to account for the characteristic size distributions of coats formed under varied conditions and, more speculatively, to contribute to the transformation of flat clathrin lattices to curved coated vesicles that are thought to occur during endocytosis.