High resolution of multiple forms of red blood cell enzymes using a Toyopearl DEAE 650 S.

We have investigated a new anion exchange chromatographic support (Toyopearl DEAE 650 S) which simultaneously allows easily to remove hemoglobin from hemolysates and to obtain a very high resolution of enzymes present in multiple forms. The results obtained are better than those obtainable using an anion-exchange HPLC column. The data obtained at analytical level suggest a wider use of this new matrix also for preparative purposes without significant changes in the resolution.     

Matrix assisted refolding of proteins by ion exchange chromatography

Two different approaches of matrix assisted refolding have been evaluated and compared to conventional refolding by dilution. Bovine alpha-lactalbumin was used for the studies as model protein. It was adsorbed under denaturing conditions on an ion exchange matrix and refolding was completed on the column prior to elution or, depending on the buffer system, in the eluate. Agarose based chromatography matrices showed high capacities for the denatured alpha-lactalbumin. A positive effect on the yield of refolded protein by the matrix could be observed for Fractogel EMD DEAE and a negative for Toyopearl DEAE 650M, DEAE Sepharose FF and Q Sepharose FF. In the case of Fractogel EMD DEAE the ion exchange surface might act as a folding helper. This property may be caused by the grafted polymers. For Source 30Q only a marginal negative influence on the refolding kinetics was observed, thus the ion exchanger is only a mean for removal of chaotropic agents. Refolding on the column is characterized by a low yield but high productivity due to significant reduction of refolding time.     

Separation of bivalent anti-T cell immunotoxin from Pichia pastoris glycoproteins by borate anion exchange

A major problem encountered in the large-scale purification of the bivalent anti-T cell immunotoxin, A-dmDT390-bisFv(G4S), from Pichia pastoris supernatants was the presence of host glycoproteins exhibiting similar charge, size, and hydrophobicity characteristics. We overcame this problem by employing borate anion exchange chromatography. The borate anion has an affinity for carbohydrates and imparts negative charges to these structures. We found that at a concentration of sodium borate between 50 and 100 mM, the nonglycosylated immunotoxin did not bind to Poros 50 HQ anion exchanger resin, but glycoproteins, including aggregates related to the immunotoxin, did. By using this property of the immunotoxin in the presence of sodium borate, we successfully developed a 3-step purification procedure: (i) Butyl-650M hydrophobic interaction chromatography, (ii) Poros 50 HQ anion exchange chromatography in the presence of borate, and (iii) HiTrap Q anion exchange chromatography. The final preparation exhibited a purity of greater than 98% and a yield of greater than 50% from the supernatant. Previously, boronic acid resins have been used to separate glycoproteins from proteins. However, combining borate anion with conventional anion exchange resins accomplishes the separation of the immunotoxin from glycoproteins and eliminates the need to evaluate nonstandard resins with respect to good manufacturing practice guidelines.     

Purification of filamentous bacteriophage M13 by expanded bed anion exchange chromatography

In this paper, we investigated the development of a simplified and rapid primary capture step for the recovery of M13 bacteriophage from particulate-containing feedstock. M13 bacteriophage, carrying an insert, was propagated and subsequently purified by the application of both conventional multiple steps and expanded bed anion exchange chromatography. In the conventional method, precipitation was conducted with PEG/NaCl, and centrifugation was also performed. In the single step expanded bed anion exchange adsorption, UpFront FastLine 20 (20 mm i.d.) from UpFront Chromatography was used as the contactor, while 54 ml (Ho = 15 cm) of STREAMLINE DEAE (rho = 1.2 g/cm3) from Amersham Pharmacia Biotechnology was used as the anion exchanger. The performance of the two methods were evaluated, analysed, and compared. It was demonstrated that the purification of the M13 bacteriophage, using expanded bed anion exchange adsorption, yielded the higher recovery percentage, at 82.86%. The conventional multiple step method yielded the lower recovery percentage, 36.07%. The generic application of this integrated technique has also been assessed.     

抗HIV融合多肽CP32M的制备工艺研究

目的:研究抗HIV融合多肽CP32M的制备工艺,为其临床前试验奠定基础。方法:采用固-液相混合策略规模合成目标肽,用离子交换色谱、反相高效液相色谱对粗肽进行纯化。结果:获得了利于提高合成及片段缩合效率的3条优选片段,CP32M粗品经DEAE离子交换色谱及C18反相纯化后纯度高于98%。结论:CP32M按3条片段(Ac-1-9-OH、Fmoc-10-21-OH、H-22-32-NH2)划分,可显著提高片段合成及缩合效率,DEAE阴离子交换色谱能除去大部分杂质,提高了第二步C18反相色谱纯化效率。     

Polyelectrolyte-coated ion exchangers for cell-resistant expanded bed adsorption

Adsorption chromatography in expanded beds is a widely used technology for direct capture of target proteins from fermentation broths. However, in many cases this method cannot be applied as a result of the strong tendency of cells or cell debris to interact with the adsorbent beads. To prevent contamination of the expanded bed with the biomass, STREAMLINE DEAE, anion exchanger designed for expanded bed adsorption, was modified with a layer of poly(acrylic acid) (PAA). The shielding layer of polyelectrolyte was attached to the surface of the matrix beads via electrostatic interactions. PAA with a high degree of polymerization was chosen to prevent diffusion of large polymer molecules into the pores of adsorbent. Thus, the shielding layer of PAA was adsorbed only at the mouth of the pores of STREAMLINE DEAE beads and only marginally decreased the binding capacity of the ion exchanger for bovine serum albumin, the model protein in this study. PAA-coated STREAMLINE DEAE practically did not interact with yeast cells, which otherwise bound strongly to the native adsorbent at neutral conditions. Cell-resistant PAA-coated anion exchanger was successfully used for isolation of BSA from the model protein mixture containing BSA, lysozyme (positively charged at applied conditions), and yeast cells. The layer of PAA was stable under mild elution conditions, and the modified adsorbent could be used in the repeated purification cycles.     

Protein degradation by the phosphoinositide-specific phospholipase C-alpha family from rat liver endoplasmic reticulum.

A 60-kDa protein homologous to phosphoinositide-specific phospholipase C-alpha was purified to apparent homogeneity on sodium dodecyl sulfate-polyacrylamide gel electrophoresis from the rough endoplasmic reticulum of rat liver through three sequential chromatographies on DEAE Toyopearl 650, AF-heparin Toyopearl 650M, and TSK gel G3000SW. The purified protein was monomeric, with an M(r) of 60,000. Eight types of protein were further separated from the 60-kDa protein and named ER60A-ER60H according to the order of their elution from a TSK gel DEAE-5PW column. They were essentially identical in terms of immunochemical properties and the NH2-terminal amino acid sequence. The partial amino acid sequence of ER60F showed homology to that of phosphoinositide-specific phospholipase C-alpha. ER60A-ER60H showed no phosphoinositide-specific phospholipase C activity. However, ER60A-ER60H catalyzed cleavage of themselves and the endoplasmic reticulum proteins protein disulfide-isomerase and calreticulin. Proteolytic degradation was inhibited by p-chloromercuribenzoate. These results indicate that ER60A-ER60H comprise a group of endoplasmic reticulum resident proteins and show thiol group-related proteolytic activity.     

Brain casein kinase 2: affinity purification procedure using immobilized polyethylenimine.

A simplified procedure for casein kinase 2 purification from bovine brain is described. The purification procedure consists of two affinity chromatography steps, using heparin and polyethylenimine immobilized on a synthetic matrix (Toyopearl 650M). The adsorption and elution conditions for each column were optimized, resulting in a simple elution protocol for each column. A stable, highly purified casein kinase 2 preparation was obtained in 4 h using this procedure. Polyethylenimine was shown to stimulate the casein kinase 2 activity using exogeneous substrates (casein, calmodulin, MAP2, and tau) but not the enzyme's autophosphorylation activity. The polyethylenimine stimulation could be overcome by applying a mass excess of the casein kinase 2 inhibitor, heparin.     

Purification and characterization of a novel isozyme of chitinase from Bombyx mori

75-kDa chitinase, which showed potential as a biocontrol agent against Japanese pine sawyer, was characterized after purification from the integument of the fifth instar larvae of Bombyx mori by chromatography on diethylaminoethyl (DEAE)-Toyoperal 650 (M), hydroxylapatite, and Fractogel EMD DEAE 650 (M) columns. The optimum pH was 6.0 toward N-acetylchitopentaose (GlcNAc5) and 10 toward glycolchitin. The optimum temperature was 60 degrees C toward GlcNAc5 and 25 degrees C toward glycolchitn. The enzyme was stable at pH 7-10 and below 40 degrees C. Kinetic analysis and reaction-pattern analysis using glycolchitin and N-acetylchitooligosacchraides as substrates indicated that 75-kDa chitinase is an endo- or random-type hydrolytic enzyme to produce the beta anomeric product and that it prefers the longer N-acetylchitooligosaccharides, suggesting, together with the N-terminal amino acid sequence, that the 75-kDa chitinase belongs to family 18 of glycosyl hydrolases.     

Toyopearl HW-65C: ammonium sulfate as a new column chromatographic adsorbent for enzyme purification

We found that Toyopearl HW-65C gel matrix adsorbed ferredoxin and ferredoxin-NADP+ reductase in the presence of concentrated ammonium sulfate. Ferredoxin was strongly adsorbed on the gel in 80% saturated ammonium sulfate, and ferredoxin-NADP+ reductase was adsorbed in 40% saturated ammonium sulfate. The phenomenon was utilized for purification of ferredoxin and the reductase on a Toyopearl HW-65C: ammonium sulfate column. The technique greatly simplified the early stage of purification of ferredoxin and the reductase. The improved purification methods further involved column treatments with DEAE-Toyopearl 650M and Matrex Red A. The effectiveness of the columns is reported. Since a number of other proteins such as cytochrome c, myoglobin, chymotrypsinogen A, ovalbumin, and glucose oxidase were also adsorbed well in an appropriately concentrated ammonium sulfate solution, the method may be of general use in enzyme purification.     

Direct recovery of glutathione S-transferase by expanded bed adsorption: anion exchange as an alternative to metal affinity fusions

The use of expanded beds of ion-exchange adsorbents for the direct recovery of a recombinant intracellular protein, glutathione S-transferase (GST), from unclarified Escherichia coli homogenates is described. The results form the basis for a comparison between this approach for purifying GST and a chelating fusion strategy and highlight the need to consider the additional costs entailed by these more-complicated approaches. The separation performance was investigated with respect to choice of anion or cation exchanger, adsorption pH, load volume, sample preparation, and stepwise elution protocol. Anion exchange was found to be more appropriate than cation exchange, as the low pHs involved in the latter caused a loss of activity. The optimal pH for adsorption was found to be 9 with a dynamic capacity from clarified homogenate in packed mode of 112 U mL(-1) (11.2 mg GST mL(-1)). As increasing volumes of unclarified homogenate were applied to the expanded bed, the yield of GST in the eluate decreased, and the purification factor was found to increase and then decrease. This was due to the displacement of weakly bound proteins by GST and then its displacement by even more strongly binding proteins. The dynamic capacity of the anion exchanger, STREAMLINE DEAE, from unclarified homogenate in expanded mode decreased slightly to 85 U mL(-1) (8.5 mg GST mL(-1)). The elution protocol for GST from the anion exchanger was then adjusted to try to maximize the degree of purification. Anion exchange expanded bed adsorption of GST from unclarified E. coli homogenate gave an eluted yield of 95.7% and 1.64-fold purification. Interestingly, a decrease in the expression level of GST in the feedstream from 23 down to 13% caused a decrease in the dynamic capacity from 85 to 14.5 U mL(-1) whereas the degree of purification remained similar.     

Separation of hexokinase activity using different hydrophobic interaction supports

Hydrophobic interaction chromatography (HIC) has been used extensively for the separation of proteins and peptides by elution using a descending salt gradient, with and without the use of detergents or denaturing agents. In this paper we compare different hydrophobic interaction chromatographic media for the separation of multiple forms of hexokinase from rabbit reticulocytes. Among the different hydrophobic chromatographic media tested (Toyopearl Phenyl 650S, Ether 650S and Butyl 650S) Toyopearl Phenyl 650S offered the best separation of multiple forms of hexokinase, probably due to its intermediate hydrophobicity. In order to establish the optimal experimental conditions, we evaluated the effects of different salts, and the results obtained demonstrated that among the antichaotropic salts, ammonium sulphate is the most suitable for the separation of hexokinase sub-types. The sample loading capacity of the three Toyopearl supports was investigated and the recovery of enzymatic activity obtained ranged from 60% to 90%, depending on the different salts and hydrophobic media used. The chromatographic profiles of hexokinase activity from various mammalian and fungal tissues also demonstrate that Toyopearl Phenyl 650S can be successfully employed for the separation of multiple forms of enzymes from different biological sources.     

PEGylated protein separation using different hydrophobic interaction supports: Conventional and monolithic supports

Protein hydrophobicity can be modified after a PEGylation process. However, hydrophobic interaction chromatography (HIC) has been used to separate PEGylation reaction products less frequently than other techniques. In this context, chromatographic monoliths represent a good alternative to continue exploring the separation of PEGylated proteins with HIC. In this work, the separation of PEGylated proteins using C4 A monolith as well as Toyopearl Butyl 650C and Butyl Sepharose was analyzed. Three proteins were used as models: RNase A, β‐lactoglobulin, and lysozyme. All proteins were PEGylated in the N‐terminal amino groups with 20 kDa methoxy poly(ethylene glycol) propionaldehyde. The concentration of ammonium sulfate (1 M) used was the same for all stationary phases. The results obtained demonstrated that the C4 A monolith could better resolve all protein PEGylation reaction mixtures, since the peaks of mono‐ and di‐PEGylated proteins can be clearly distinguished in the chromatographic profiles. On the contrary, while using Butyl Sepharose media only the PEGylation reaction mixtures of RNase A could be partially separated at 35 and 45 CVs. PEGylated proteins of β‐lactoglobulin and lysozyme could not be resolved when Toyopearl Butyl 650C and Butyl Sepharose were used. It is then clear that monoliths are an excellent choice to explore the purification process of PEGylated proteins exploiting the advantages of HIC. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:702–707, 2016     

Comparative analysis of the methods used for finding surface energy to investigate protein interaction behavior on chromatographic supports

Hydrophobic interaction chromatography, an important and effective purification strategy, is generally used for the purification of variety of biomolecules. A basic understanding of the protein interaction behavior is required to effectively separate these biomolecules. A colloidal type extended Derjaguin, Landau, Verwey, and Overbeek calculations were utilized to study the interactions behavior of model proteins to commercially available hydrophobic chromatographic materials that is, Toyopearl Phenyl 650C and Toyopearl Butyl 650C. Physicochemical properties of selected model proteins were achieved by contact angle and zeta potential measurements. The contact angle of chromatographic materials used was achieved through sessile drop method on disrupted beads and capillary penetration method (CPM) on intact beads. The surface properties were further used to calculate the interactions of the proteins to chromatographic supports. The calculated secondary energy minimum of the proteins with the chromatographic materials (from the contact angle values determined through both methods can be correlated with the retention volumes from the real chromatography. The secondary energy minimum values are higher for each protein to the chromatographic materials calculated from the inputs derived through sessile drop method compared to CPM. For instance, immunoglobulin G has secondary energy minimum value of 0.17 kT compared to 0.11 kT, obtained through sessile drop method and CPM, respectively. Average relative values of the energy minimum calculated for all proteins are as 1.51 kT and 1.29 kT for Toyopearl Butyl 650C and Toyopearl Phenyl 650C, respectively, as a conversion factor for estimation of secondary energy minimum for both methods.     

Purification and characterization of a novel thermostable lipase from Bacillus sp

A thermostable lipase from Bacillus sp. has been purified to homogeneity as judged by disc-PAGE, SDS-PAGE, and isoelectric focusing. The purification included ammonium sulfate fractionation, treatment with acrinol, and sequential column chromatographies on DEAE-Sephadex A-50, Toyopearl HW-55F, and Butyl Toyopearl 650M. The purified enzyme was found to be a monomeric protein with Mr of 22,000, and pI of 5.1. The optimal pH at 30 degrees C, and optimal temperature at pH 5.6 were 5.5-7.2, and 60 degrees C, respectively, when olive oil was used as the substrate. The substrate specificity towards simple triglycerides was broad and 1- and 3-positioned ester bonds were hydrolyzed in preference to a 2-positioned ester bond. The addition of acetone to the assay mixture in the range of 0-60% (v/v) stimulated the enzyme remarkably, whereas n-hexane had an inhibitory effect.     

Adsorption Behavior of Multicomponent Protein Mixtures Containing α1−Proteinase Inhibitor with the Anion Exchanger, 2-(Diethylamino) ethyl-Spherodex

The equilibrium binding behavior of α₁-proteinase inhibitor (α₁-PI) in the presence of human serum albumin (HSA) has been determined in packed bed systems with the anion exchanger, 2-(diethylamino) ethyl (DEAE) -Spherodex. Experimental data derived for the individual proteins were compared with the corresponding data obtained from batch adsorption studies as well as studies in which mixtures of these two proteins were loaded at different concentration ratios onto columns of the same anion exchange adsorbent. The results confirm that α₁-PI has a greater affinity for the anion exchanger, although competitive adsorption was observed as the inlet concentration of HSA was increased. Under these conditions, decreased binding capacities and lower dynamic adsorption rates were observed for α₁-PI with the DEAE-Spherodex anion exchange adsorbent. The results are discussed in terms of the influence which various contaminants that occur in multicomponent mixtures of proteins from human plasma can have on the equilibrium binding characteristics of a target protein with weak or strong ion exchange adsorbents under conditions approaching concentration overload in preparative chromatographic systems. These investigations have also addressed, as the first part of an iterative approach for the simulation of the adsorption behavior of multicomponent mixtures of human plasma proteins with ion exchange and affinity chromatographic adsorbents, the ability of noncompetitive and competitive Langmuirean models to simulate the adsorption of α₁-PI in the presence of different concentrations of HSA to DEAE-Spherodex.     

Cation-exchange chromatography of monoclonal antibodies: Characterisation of a novel stationary phase designed for production-scale purification

A novel cation-exchange resin, Eshmuno? S, was compared to Fractogel® SO3- (M) and Toyopearl GigaCap S-650M. The stationary phases have different base matrices, and carry specific types of polymeric surface modifications. Three monoclonal antibodies (mAbs) were used as model proteins to characterize these chromatographic resins. Results from gradient elutions, stirred batch adsorptions and confocal laser scanning microscopic investigations were used to elucidate binding behaviour of mAbs onto Eshmuno? S and Fractogel® SO3- and the corresponding transport mechanisms on these two resins.

The number of charges involved in mAb binding for Eshmuno? S is lower than for Fractogel® SO3-, indicating a slightly weaker electrostatic interaction. Kinetics from batch uptake experiments are compared to kinetic data obtained from confocal laser scanning microscopy images. Both experimental approaches show an accelerated protein adsorption for the novel stationary phase. The influence of pH, salt concentrations and residence times on dynamic binding capacities was determined. A higher dynamic binding capacity for Eshmuno? S over a wider range of pH values and residence times was found compared to Fractogel® SO3- and Toyopearl GigaCap S-650M.

The capture of antibodies from cell culture supernatant, as well as post-protein A eluates, were analyzed with respect to their host cell protein (hcp) removal capabilities. Comparable or even better hcp clearance was observed at much higher protein loading for Eshmuno? S than Fractogel® SO3- or Toyopearl GigaCap S-650M.     

Purification, Characterization, and Immunological Properties of NADH-Dependent Glutamate Synthase from Rice Cell Cultures

To obtain a monospecific antibody against NADH-dependent glutamate synthase (NADH-GOGAT; EC 1.4.1.14), the enzyme was purified to homogeneity from cultured rice cells (Oryza sativa) with column chromatography using Butyl Toyopearl 650M, Sephacryl S-300, Blue Sepharose CL-6B, and Butyl Toyopearl 650S. The specific activity at the final stage of the purification was 9.8 micromoles of glutamate formed per minute per milligram of protein. The yield was 6.1% and purification was 815-fold. Analysis by denaturing gel electrophoresis revealed a single polypeptide with an apparent molecular weight of 196,000, similar to the value of 194,000 estimated for the native protein. Apparent K_m values for l-glutamine, 2-oxoglutarate, and NADH were 811, 76, and 3.0 micromolar, respectively. Neither NADPH nor l-asparagine substituted for NADH and l-glutamine, respectively. The enzyme had its absorption maxima at 273, 373, and 440 nanometers with a shoulder at 475 nanometers, suggesting that the rice NADH-GOGAT is a flavoprotein. Monospecific antibody raised against NADH-GOGAT purified from the rice cells was obtained as the first instance for the enzyme in higher plants. Immunological analyses showed that the antibody for rice cell NADH-GOGAT reacted with only the enzyme in extracts from the cells. The anti-NADH-GOGAT antibody did not recognize the ferredoxin-GOGAT purified from rice leaves, and likewise the anti-rice leaf ferredoxin-GOGAT antibody did not react with the NADH-GOGAT purified from the cultured rice cells.     

Purification of a Latent Form of Polyphenoloxidase from La France Pear Fruit and Its Pressure-activation

A latent form, mostly soluble, of polyphenoloxidase of La France pear fruit (Pyrus communis) was purified to homogeneity by ammonium sulfate fractionation and anion-exchange chromatography with DEAE-Sephadex A-25 and then DEAE-Toyopearl 650M, followed by gel permeation chromatography with Toyopearl HW-55s. The addition of 10% glycerol to the eluting buffer was needed for purification. The purified latent enzyme seemed to be a monomeric protein; the molecular weight was estimated to be 70,000 by gel permeation chromatography and 65,000 by SDS–polyacrylamide gel electrophoresis. The enzyme was activated by pressurization at 400 MPa or higher or by treatment with SDS. The highest activity was obtained by pressurization at 600 MPa and 20°C for 6 h.