The extractive purification of peroxidase from plant raw materials in aqueous two-phase systems

The extractive purification of peroxidase from Armoracia rusticana roots and Glycine max seed coats in temperature-induced and affinity microsphere-containing aqueous two-phase systems was stuied. The extractive purification of peroxidase from Glycine max seed coats was carried out in a temperature-induced aqueous two-phase system formed by Triton X-45, Triton X-100 and sodium acetate at pH 5.5 A 99% yield with a 6-fold purification factor was obtained. When the clear top phase was subjected to concanavalin-A affinity chromatography, the purification factor rose to 41 and the yield dropped to 28%. A two-step purification process for peroxidase from Armoracia rusticana roots was developed by adding concanavalin-A affinity microspheres to a PEG/phosphate aqueous two-phase system. The method allows a 60% recovery of high purity peroxidase (1,860 guaiacol units per mg). A lower recovery rate and degree of purification of this enzyme was achieved after temperature-induced aqueous two-phase partition or acetone precipitation and concanavalin-A affinity column chromatography.     

Comparison of human thyroxine-binding globulin purification by affinity chromatography procedures

Three procedures for the isolation of thyroxine-binding globulin from human serum, using affinity chromatography on triiodothyronine (T3) linked to Sepharose (A), thyroxine (T4) linked to Sepharose (B) or T3 linked to epoxy-Sepharose (C) as the first purification step, were compared. With the use of additional purification steps, the three procedures yielded pure thyroxine-binding globulin without desialylation. With procedure A, the initial binding of T4-binding globulin to T3-Sepharose was very low, yielding a poor final recovery (17%). Procedure B gave the highest yield (35%) after a three-step purification, with a low T4 content (0.15-0.30 mol/mol). Procedure C also gave a high yield (28%) after only two purification steps, with a T4 content greater than 0.7 mol/mol. The microheterogeneity of T4-binding globulin obtained with these three procedures was demonstrated by isoelectric focusing: five major bands were observed between pH 4.1 and 4.6, and intermediate faint bands (often doublets) in the same pH range. However, with procedures A and C, the most acidic bands (pH 4.10-4.20) were always absent. Thyroxine-binding globulin was preincubated with radioactively labelled T3 or T4 and the hormone-protein complex was analyzed by isoelectric focusing. The binding of T3--compared to that of T4--was reduced in the most acidic protein subspecies. These results suggest differences in the thyroid hormone binding properties of the various subspecies of human T4-binding globulin.     

Extracellular enzyme system utilized by the fungus Sporotrichum pulverulentum (Chrysosporium lignorum) for the breakdown of cellulose. 3. Purification and physico-chemical characterization of an exo-1,4-beta-glucanase.

An exo-1,4-beta-glucanase from culture solution of the rot fungus Sporotrichum pulverulentum (formerly called Chrysosporium lignorum) grown on powder cellulose as the sole carbon source has been extensively purified and characterized with respect to some physico-chemical properties. The purification has been carried out in a five-step procedure comprising chromatography on DEAE-Sephadex, gel filtration on polyacrylamide P-150, activation on a Dowex 2-X8 anion exchanger, chromatography on Concanavalin A-Sepharose and chromatography on SP-Sephadex. The purified enzyme was found to be pure and homogeneous by analytical polyacrylamide electrophoresis, by electrophoresis on dodecylsulphate gels and by analytical polyacrylamide electrophoresis, by electrophoresis on dodecylsulphate gels and by analytical isoelectric focusing. A single symmetrical peak was obtained with the free zone electrophoresis method. The purification factor is about 15 and the yield of exo-1,4-beta-glucanase activity 7%. After purification, the enzyme showed no viscosity-decreasing activity towards carboxymethyl-cellulose solutions. The exo-1,4-beta-glucanase was isoelectric at pH 4.3 (4 degrees C). A molecular weight of 48600 was calculated on the basis of a knowledge of the partial specific volume, ultracentrifugation data and the amino acid composition. The enzyme contained no carbohydrate.     

Recombinant protein purification using complementary peptides as affinity tags

Affinity tags have become highly popular tools for purifying recombinant proteins from crude extracts by affinity chromatography. Besides, short peptides are excellent ligands for affinity chromatography, as they are not likely to cause an immune response in case of leakage into the product, they are more stable than antibodies to elution and cleaning conditions and they usually have very acceptable selectivity. Hydropathically complementary peptides designed de novo show enough selectivity to be used successfully as peptide ligands for protein purification from crude extracts. Recognition specificity and selectivity in the interaction between the complementary peptide pair His-Leu-Leu-Phe-Pro-Ile-Ile-Ile-Ala-Ala-Ser-Leu and Lys-Asn-Tyr-Pro-Lys-Lys-Lys-Met-Glu-Lys-Arg-Phe have been demonstrated by other authors. In this work, we designed a recombinant protein purification method using a peptide affinity tag that binds to a peptide-binding partner immobilized on a chromatographic matrix. The enhanced green fluorescent protein expressed (EGFP) in Escherichia coli was used as the model. The peptide Gly-Gly-Gly-His-Leu-Leu-Phe-Pro-Ile-Ile-Ile-Ala-Ala-Ser-Leu was synthesized by solid phase using the Fmoc chemistry and immobilized in NHS-Sepharose (PC-Sepharose). Gly residues were added as a spacer arm at the N terminus. The EGFP was expressed either with the fusion tag Lys-Asn-Tyr-Pro-Lys-Lys-Lys-Met-Glu-Lys-Arg-Phe on the C terminus (EGFP-CPTag) or without any fusion tag. After cell disruption, the extract was directly applied to the PC-Sepharose column equilibrated with 20mM sodium phosphate buffer, pH 7.0. The adsorbed EGFP-CPTag was then eluted with 1M Tris. The yield was 98% and the purification factor 4.6. By contrast, EGFP without tag pass through without interacting with the PC-Sepharose column. The method designed can be applied for the purification of other recombinant proteins.     

Purification and characterization of an abscisic acid-inducible anionic peroxidase associated with suberization in potato (Solanum tuberosum)

An anionic peroxidase (EC 1.11.1.7), thought to be involved in suberization, was purified 110-fold from wound-healing slices of Solanum tuberosum by a combination of ammonium sulfate fractionation, Sephadex G-100 gel filtration, isoelectric focusing, and phenyl-Sepharose CL-4B chromatography in 24% yield. The purified enzyme was homogeneous as judged by sodium dodecyl sulfate-polyacrylamide gel electrophoresis and horizontal thin-layer polyacrylamide gel electrophoresis. The molecular weight of the enzyme was estimated to be 47,000 by both Sephadex G-100 gel filtration and sodium dodecyl sulfate-polyacrylamide gel electrophoresis. This peroxidase was found to be a glycoprotein containing about 17% carbohydrate, approximately one-quarter of which was shown to be glucosamine residues. It was found to have an isoelectric point of 3.15. An anionic peroxidase was also isolated from abscisic acid-treated callus tissue culture of S. tuberosum by the above purification procedure. The two enzymes were shown to be immunologically similar, if not identical, based on their cross-reactivity with rabbit antibody prepared against the peroxidase from wound-healing slices, whereas the major cationic peroxidase from wound-healing slices did not cross-react with this antibody. The anionic enzyme from both sources showed very similar specific activities when assayed with a range of substrates, whereas the specific activities found for the cationic isozyme isolated from wound-healing slices were quite different.     

Purification of ram seminal plasma acid alpha-glucosidase

1. Ram seminal plasma alpha-glucosidase has been purified in order to increase our knowledge of this enzyme and of its role in epididymal physiology. 2. Since the enzyme behaved differently from other known acid alpha-glucosidases and was not affinity-adsorbed on dextran gels, another approach had to be used. 3. The final procedure included an ethanol precipitation step, sequential chromatography on hydroxylapatite and DEAE Sepharose CL-6B, isoelectric focusing in polyacrylamide gels and ultrafiltration. 4. The resulting purification factor of alpha-glucosidase was 9822 with an overall yield of 5%. 5. The purified material consisted of several isoforms with a mol. wt of 105,000 and isoelectric points varying between 4 and 5.     

Expression of human insulin-like growth factor I in bacteria: use of optimized gene fusion vectors to facilitate protein purification

Several fusions between the gene for human insulin-like growth factor I (IGF-I) and the genes for different IgG-binding fragments of staphylococcal protein A were assembled and compared regarding expression, secretion, and purification of the peptide hormone. After IgG affinity purification of the fusion proteins from the growth medium of Staphylococcus aureus or Escherichia coli, native IGF-I was released by cleavage of an Asn-Gly peptide bond with hydroxylamine. An optimized expression system based on a modified synthetic IgG-binding domain (z), resistant to hydroxylamine, gave the highest yield of fusion protein. After cleavage, the hormone could be separated from the IgG-binding moiety and from noncleaved fusion protein by a second passage through the IgG affinity column. The biological activity and the purity of the IGF-I obtained were confirmed by a radioreceptor assay, N-terminal sequence analysis, polyacrylamide gel electrophoresis, isoelectric focusing, and high-performance liquid chromatography.     

Methods for preparation of low abundance glycoproteins from mammalian cell supernatants

Proteins secreted to mammalian cell supernatants are usually in a low concentration and purity, due to the limitation of the expression systems or the presence of a large amount of contaminant proteins from the cell medium. So, initial protein recovery from cell supernatants requires of a highly specific chromatography step. We compared several purification methods based on affinity chromatography for purification of proteins from cell culture supernatants: metal chelate affinity, strep-tag and immunopurification with a monoclonal antibody. Soluble receptor glycoproteins were engineered with the corresponding peptide tag at their C-terminal end. The proteins were expressed in 293T cells and secreted to the cell supernatant, as monitored by sandwich ELISA. Supernatants were run through the different chromatography columns and several purification-related parameters determined. While all column-retained proteins were easily eluted, the chelating and immunopurification chromatography gave the highest yield and the latest method provided a sample with the highest purity. So, in spite of its cost, immunopurification chromatography gave optimal results for purification of a low abundance protein from a cell supernatant. Finally, we applied a protein expression system together with immunopurification chromatography for preparation of a glycoprotein for crystallization.     

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.     

Demonstration and partial purification of lactoperoxidase from human colostrum

A peroxidase with stability, chromatographic and immunoreactive properties similar to that of bovine lactoperoxidase has been partly purified from human colostrum. Hydrophobic interaction chromatography on Phenyl-Sepharose C1-4B gave a 10-fold purification with an apparent recovery of about 45%. The enzyme was quantitatively and specifically adsorbed to beads of anti-lactoperoxidase (bovine)-Protein A-Sepharose. No adsorption of the enzyme was observed on immunoadsorbent columns prepared with high-titre polyclonal antibodies raised against human myeloperoxidase and human eosinophile peroxidase.     

Purification and characterization of human kidney renin

By means of a new rapid and small scale purification method, human kidney renin has been purified from a single kidney in a homogeneous state, as judged on SDS-PAGE. The kidney which showed unusually high renin activity was from a patient with cardiomyopathy. 8,000-fold purification was attained by means of only pepstatin-aminohexyl-Sepharose chromatography and FPLC on a Mono Q column, and the yield was 34%. The specific activity was 5.63 mg angiotensin I per mg protein per h at 37 degrees C and pH 6.5 with porcine angiotensinogen as the substrate. The molecular weight was estimated to be 37,000 by SDS-PAGE and 38,000 by HPLC on a TSK G-3000 SW column. The preparation showed three bands on isoelectric focusing. The molecular weight and the profile on isoelectric focusing of the purified renin agreed with those found for the extracts of both the patient's kidney and a kidney with the usual low renin activity.     

Fractionation of horseradish peroxidase by preparative isoelectric focusing, gel chromatography and ion-exchange chromatography.

Horseradish peroxidase has been fractionated by preparative isoelectric focusing in a density gradient and in a layer of granulated gel using pH-3-10 and narrow-pH-range carrier ampholytes at different total enzyme loads. The resolution of peroxidase isoenzymes in preparative-layer isoelectric focusing was comparable to that obtained by analytical thin-layer isoelectric focusing. Isoelectrically homogeneous isoenzymes could be isolated with good recovery in a single fractionation step. Despite the excellent separation of the individual isoenzymes by isoelectric focusing in gel layers, an effective purification, indicated by the absorbance ratio A403mn/A278nm, could not be achieved by focusing applied as a single step. By different fractionation sequences combining gel chromatography, ion-exchange chromatography, and isoelectric focusing, individual isoenzymes with a high purity and homogeneous with respect to their size and charge properties have been isolated.     

One-step purification and structural characterization of a recombinant His-tag 11S globulin expressed in transgenic tobacco

Amarantin, an 11S globulin, is one of the most important storage proteins of amaranth seeds, with relevant nutritional-functional and nutraceutical characteristics. Its cDNA was cloned in-frame with a sequence encoding a polyhistidine tag and expressed under the direction of a 35S promoter in transgenic tobacco seeds. The presence of a (His)(6) tag on the polypeptide permitted a high-yield single-step purification using immobilized metal-ion affinity chromatography and rapid characterization. Purified His-tag amarantin accounted for up to 5% of total soluble seed protein. Biochemical characterization indicated that purified His-tag amarantin migrated with the expected molecular weight (53 kDa) and was correctly processed into an acidic polypeptide (32 kDa) with isoelectric point (pI) of 5.58 and a basic polypeptide (21 kDa) with pI of 9.24, linked by a disulfide bridge. Moreover, His-tag amarantin was assembled into both homo- and hetero-hexameric 11S structures. These results show that the His tag did not change the biochemical and physicochemical properties of amarantin. The strategy presented here for rapid and high-yield expression and purification procedure should facilitate structure-function studies for this nutritional protein.     

Influence of tryptophan tags on the purification of cutinase, secreted by a recombinant Saccharomyces cerevisiae, using cationic expanded bed adsorption and hydrophobic interaction chromatography

During cationic bed adsorption (EBA), with cutinase with varying length tryptophan tags (WP)(2)and (WP)(4), 33% and 10% of adsorption capacity and 80% and 32% eluted specific activity were observed in relation to wild type (wt)-cutinase in the conventional process. Therefore, as the hydrophobicity of the protein increases, it is important to integrate the EBA step with a hydrophobic interaction chromatography (HIC) process. As the length of the hydrophobic tag-(WP) increases from n = 2 to n = 4, the purification factor obtained by HIC was 1.8 and 2.2-fold higher than wt-cutinase. However, the recovery yield obtained in HIC decreases substantially as the length of hydrophobic tag increases (97%, 84% and 70% for wt-cutinase, cutinase-(WP)(2) and cutinase-(WP)(4)). The integration of two purification steps, EBA followed by HIC, resulted in the highest overall purity level for cutinase-(WP)(2), and the highest overall recovery yield for wt-cutinase. When optimizing the design of a hydrophobic tag fused to a protein secreted by Saccharomyces cerevisiae it must be considered that the cultivation parameters could impair the downstream process, and consequently the optimum tag is not necessarily the one that presents the highest purification factor in HIC.     

Large-scale purification of staphylococcal enterotoxins A, B, and C2 by dye ligand affinity chromatography

A simple method for the purification of staphylococcal enterotoxins A (SEA), B (SEB), and C2 (SEC2) from fermentor-grown cultures was developed. The toxins were purified by pseudo-affinity chromatography by using the triazine textile dye "Red A" and gave overall yields of 49% (SEA), 44% (SEB), and 53% (SEC2). The purified toxins were homogeneous when analyzed by sodium dodecyl sulfate-polyacrylamide gel electrophoresis, but isoelectric focusing of the preparations revealed the microheterogeneity associated with these toxins. The SEA and SEB preparations each consisted of two isoelectric forms with pI values of 7.3 and 6.8 (SEA) and 8.9 and 8.55 (SEB); in contrast, SEC2 contained five different isoelectric forms, with pI values ranging between 7.6 and 6.85. The pattern of elution of the isoelectric forms from the column indicated a cationic-exchange process involved in the binding of toxin to Red A. Such a method forms the basis of a high-yielding, rapid means of purifying the staphylococcal enterotoxins that can easily be adapted to large-scale production.     

Purification and characterization of the individual glutathione S-transferases from sheep liver

The glutathione S-transferases (EC 2.5.1.18) have been purified to electrophoretic homogeneity from 105,000g supernatant of sheep liver homogenate by employing a combination of gel filtration on Sephadex G-150 and affinity chromatography on S-hexylglutathione-linked Sepharose-6B columns. Approximately 70% of the original glutathione S-transferase activity toward 1-chloro-2,4-dinitrobenzene and glutathione peroxidase activity toward cumene hydroperoxide could be recovered by this purification method. Of particular importance in developing this procedure was the fact that the enzyme preparation obtained after affinity column chromatography represented all the isozymes of sheep liver glutathione S-transferases. Further purification by CM-cellulose and DEAE-cellulose column chromatography resolved the glutathione S-transferases into seven distinct cationic isozymes designated C-1, C-2, C-3, C-4, C-5, C-6, and C-7 and five overlapping anionic transferases designated A-1, A-2, A-3, A-4, and A-5, respectively, in the order of their elution from the ion-exchange columns. The sodium dodecyl sulfate SDS-gel electrophoretic data on subunit composition revealed that cationic enzymes are composed of two subunits with an identical Mr of 24,000 whereas a predominant subunit with Mr of 26,000 was observed in all anionic isozyme peaks except A-1. Cationic isozymes accounted for approximately 98% of the total peroxidase activity associated with the glutathione S-transferase whereas only A-1 of the anionic isozymes displayed some peroxidase activity. Isozyme C-4 was found to be the most abundant glutathione S-transferase in the sheep liver. Characterization of the individual transferases by their specificity toward a number of selected substrates, subunit composition, and isoelectric points showed some similarities to those patterns for human liver glutathione S-transferases.     

Purification and some properties of ornithine decarboxylase from rat liver

Ornithine decarboxylase (EC 4.1.1.17) was purified to near homogeniety from livers of thioacetamide- and dl-α-hydrazino-δ-aminovaleric acid-treated rats by using three types of affinity chromatography with pyridoxamine phosphate-Sepharose, pyridoxamine phosphate-dipropylenetriamine-Sepharose and heparin-Sepharose. This procedure gave a purification of about 3.5·10⁵-fold with an 8% yield; the specific activity of the final enzyme preparation was 1,1·10⁶ nmol CO₂/h per mg protein. The purified enzyme gave a single band of protein which coincided with activity peak on polyacrylamide gel electrophoresis and also gave a single major band on SDS-polyacrylamide gel electrophoresis. A single precipitin line was formed between the purified enzyme and an antiserum raised against a partially purified enzyme, on Ouchterlony immunodiffusion. The molecular weight of the enzyme was estimated to be 105 000 by polyacrylamide gel electrophoresis at several different gel concentrations; the dissociated subunits had molecular weights of 50 000 on SDS-polyacrylmide gels. The isoelectric point of the enzyme was pH 4.1.     

Large-scale purification of staphylococcal enterotoxins A, B, and C2 by dye ligand affinity chromatography.

A simple method for the purification of staphylococcal enterotoxins A (SEA), B (SEB), and C2 (SEC2) from fermentor-grown cultures was developed. The toxins were purified by pseudo-affinity chromatography by using the triazine textile dye "Red A" and gave overall yields of 49% (SEA), 44% (SEB), and 53% (SEC2). The purified toxins were homogeneous when analyzed by sodium dodecyl sulfate-polyacrylamide gel electrophoresis, but isoelectric focusing of the preparations revealed the microheterogeneity associated with these toxins. The SEA and SEB preparations each consisted of two isoelectric forms with pI values of 7.3 and 6.8 (SEA) and 8.9 and 8.55 (SEB); in contrast, SEC2 contained five different isoelectric forms, with pI values ranging between 7.6 and 6.85. The pattern of elution of the isoelectric forms from the column indicated a cationic-exchange process involved in the binding of toxin to Red A. Such a method forms the basis of a high-yielding, rapid means of purifying the staphylococcal enterotoxins that can easily be adapted to large-scale production.