Fractionation of lignin-carbohydrate complexes by hydrophobic-interaction chromatography

Hydrophobic properties of lignin-carbohydrate complexes (LCC) isolated from Pinus densiflora Sieb. et Zucc. have been analysed by hydrophobic-interaction chromatography on Phenyl- and Octyl-Sepharose CL-4B gels. The ability of LCC to be adsorbed by these hydrophobic gels was exclusively dependent on their lignin content. Materials adsorbed on Octyl-Sepharose were desorbed with a lower concentration of 2-ethoxyethanol than those adsorbed on Phenyl-Sepharose. In the adsorption of LCC by Phenyl-Sepharose, ππ interactions between the aromatic ligands and the benzene skeletons of lignin play an important role, whereas hydrophobic interaction is the exclusive driving-force for adsorption in the case of Octyl-Sepharose.     

Thiophilic adsorption: a comparison of model protein behavior

A newly recognized type of protein-ligand interaction phenomenon has resulted in the preparation of simple, nonionic, and highly specific gel derivatives for selective adsorption chromatography. The essential structure of the immobilized ligand can be represented as agarose-CH2CH2SO2CH2CH2SCH2CH2OH, which was prepared by using mercaptoethanol to derivatize [0.9-1.0 mmol (g of dry gel)-1] divinyl sulfone activated agarose (thiophilic or T-gel). Proteins interacting with this ligand are provisionally termed "thiophilic" to recognize their affinity for the definitive sulfone-thioether constituents. To better understand the experimental variables affecting adsorption efficiency and selectivity, several well-characterized proteins with diverse physicochemical features have been evaluated for thiophilic properties. Thiophilic interaction chromatography was investigated as a function of pH as well as the type and concentration of water-structure-forming salts required to promote adsorption. The model proteins characterized varied distinctly in their individual thiophilic affinities. At acidic pH values, a salt-independent adsorption process was observed. Furthermore, a minimum in the salt-promoted thiophilic adsorption tendency at pH 5-6 was found, with varying magnitude, for each of the model proteins evaluated. Recovery of adsorbed proteins routinely varied from 90% to 100%. There does not appear as yet to be any easily recognized physicochemical property associated with either thiophilic or nonthiophilic behavior. These results suggest that thiophilic interaction chromatography is a process that utilizes a previously unrecognized protein-ligand interaction mechanism. We suggest that salt allows the protein into close proximity with the sulfone-thioether group where short-range forces are effective.(ABSTRACT TRUNCATED AT 250 WORDS)     

Evaluation of modified chitosan as matrix for hydrophobic interaction chromatography

Chitosan beads were modified with glutaraldehyde and modified chitosan was investigated as matrix for hydrophobic interaction chromatography. The influence of temperature, type of salt and its ionic strength on the adsorption of -galactosidase was studied. -Galactosidase was found to bind in presence of high concentration of ammonium sulphate (3 M, w/v) and 90% of the bound enzyme was eluted with decreasing salt concentration in presence of 10% ethylene glycol. Attempt was made to purify -galactosidase from modified chitosan, -galactosidase showed 1.7-fold purification with 43.96% recovery of enzyme activity. The SDS–PAGE analysis of enzyme showed considerable purification and its molecular weight was found to be 63–64 kDa. Unlike other chromatographic matrices, the prepared chitosan beads were used five times. The results showed that purification and recovery of the enzyme did not change even when column size was increased.     

Hydrophobic chromatography and fractionation of enzymes from extremely halophilic bacteria using decreasing concentration gradients of ammonium sulfate.

Ammonium sulfate fractionation of proteins from extremely halophilic bacteria on Sepharose 4B, carboxymethylcellulose, diethylaminoethylcellulose, and hexamethylenediamine-Agarose is described. Halophilic proteins are absorbed on these gels at 2.5 M ammonium sulfate and eluted by decreasing concentration gradients of this salt. The method has enabled the separation of malate dehydrogenase from glutamate dehydrogenase and aspartate aminotransferase on Sepharose 4B and the additional 15-fold purification of glutamate dehydrogenase on DEAE-cellulose. The technique is simple and convenient, operates at low cost, and possesses great power of resolution. The mechanism of adsorption is discussed and compared to previous instances of "hydrophobic chromatography". It is concluded that the retention of halophilic proteins on the polysaccharide gels at 2.5 M ammonium sulfate is due to hydrophobic interactions.     

Protein instability during HIC: hydrogen exchange labeling analysis and a framework for describing mobile and stationary phase effects

Unfolding of marginally stable proteins is a significant factor in commercial application of hydrophobic interaction chromatography (HIC). In this work, hydrogen-deuterium isotope exchange labeling has been used to monitor protein unfolding on HIC media for different stationary phase hydrophobicities and as a function of ammonium sulfate concentration. Circular dichroism and Raman spectroscopy were also used to characterize the structural perturbations experienced by solution phase protein that had been exposed to media and by protein adsorbed on media. As expected, greater instability is seen on chromatographic media with greater apparent hydrophobicity. However, increased salt concentrations also led to more unfolding, despite the well-known stabilizing effect of ammonium sulfate in solution. A thermodynamic framework is proposed to account for the effects of salt on both adsorption and stability during hydrophobic chromatography. Using appropriate estimates of input quantities, analysis with the framework can explain how salt effects on stability in chromatographic systems may contrast with solution stability.     

Thiophilic adsorption chromatography: purification of Equ c2 and Equ c3, two horse allergens from horse sweat

Purification of two allergens from horse (Equus caballus) sweat, Equ c2 and Equ c3, by means of salt-promoted chromatography on a “thiophilic” (T-gel) adsorbent is described. Immobilization of these proteins was found to be dependent on the presence of water-structure-forming salts where the ammonium sulphate concentration in the equilibration buffer was 2 M. Equ c2 showed higher affinity towards the thiophilic matrix than Equ c3. Their molecular mass (M_r) values established by SDS–polyacrylamide gel electrophoresis were for Equ c2 ≈17 000 and for Equ c3 ≈16 000, and both proteins showed a low isoelectric point of ≈3.8. Their allergenic properties were also investigated using sera from horse-sensitized patients, where it was demonstrated that these proteins exhibited an IgE antibody binding capacity. In this report we show the broad potential applications of thiophilic adsorption chromatography for the efficient purification of allergens.     

Recovery of c-phycocyanin from the cyanobacteriumSpirulina maxima

Spirulina biomass was separated into two fractions which may have various uses. A phycocyanin fraction may provide a food colourant and biomarkers, and a protein-rich leftover may be useful as aquaculture feed. Activated charcoal adsorption, ultrafiltration and spray drying were used effectively to produce a high quality colourant grade phycocyanin, while activated charcoal adsorption, ammonium sulphate precipitation, dialysis and chromatography were effective in preparing reagent grade phycocyanin.     

General aspects of hydrophobic chromatography. Adsorption and elution characteristics of some skeletal muscle enzymes.

If the degree of substitution of Sepharose 4 B with alpha-alkylamines is varied gels of different hydrophobicity are produced. Proteins can be adsorbed when a critical hydrophobicity (ca. 10-12 alkyl residues/Sepharose sphere) is reached. The enzymes phosphorylase kinase, phosphorylase phosphatase, 3',5'-cAMP dependent protein kinase, glycogen synthetase, and phosphorylase b are successively adsorbed as the hydrophobicity of the Sepharose is increased. The capacity of the gels for these enzymes and protein in general increases exponentially reaches plateau values as a function of the degree of substitution. There is no indication of a restriction of the hydrophobic centers for a given protein. The critical hydrophobicity needed to adsorb proteins can either be otained in the above manner or by elongation of the employed alkylamine at a constant degree of substitution. Additonally, as the hydrophobicity of a gel is increased higher binding forces result and desorption of proteins requires an augmentation of the salt concentration in the elution buffer. Elution of proteins from a hydrophobic matrix can be described in terms of salting-in phenomena since desorption is dependent on the type of salt employed and not on the ionic strength alone. This also rules out ionic interactions as a major factor in adsorption per se. By rationally controlling the hydrophobicity of a Sepharose gel the adsorption and elution of a protein may be thus establised that its purification or elimination can be optimally performed.     

Extracellular Lytic Enzymes of Myxococcus virescens II. Purification of Three Bacteriolytic Enzymes and Determination of their Molecular Weights and Isoelectric Points

The bacteriolytic enzymes produced by Myxococcus virescens and previously concentrated and separated from most of the non-bacteriolytic proteins have been further separated and purified. The bacteriolytic enzyme solution was concentrated by lyo-philization. When applied to a Sephadex G-100 column, three peaks of bacteriolytic activity were eluted. Polyacrylamide gel electrophoresis showed that all the three enzyme fractions were contaminated with at least four non-bacteriolytic proteins. In the first enzyme fraction the bacteriolytic enzymes could be freed from the contaminating proteolytic activity by adsorption on a hydroxylapatite column. The bacteriolytic enzymes could then be adsorbed on a CM-cellulose column. The remaining contaminating proteins passed the column un-adsorbed while the bacteriolytic enzymes could be eluted with a gradient of 0.02–0.10 M ammonium hydrogen carbonate solution. The second enzyme fraction was adsorbed on a CM-cellulose column and then eluted with 0.03–0.15 M NH4 HCO₃. After rechromatography on a new column under the same conditions, all of the contaminating proteins had disappeared. For purification of the third enzyme fraction chro-matography on one single CM-cellulose column was sufficient. The elution of the adsorbed enzymes was performed with a gradient of 0.15–0.30 M NH₄HCO₃. The recovery of activity for each of the ion-exchange chromatography separations was at least 90%. The purity of the enzymes was tested by polyacrylamid gel electrophoresis. Each of the purified enzymes gave only one coloured band which coincided with the enzyme activity assayed in sliced gels. The molecular weights of the enzymes were determined by electrophoresis on acryl-amide gels containing sodiumdodecylsulphate. The molecular weights determined in this way (about 40,000, 30,000 and 20,000, respectively) were about 10,000 daltons higher than those obtained by gel chromatography on Sephadex G-100. This discrepancy seems to depend on interactions between the enzymes and the dextran molecules probably caused by the strongly basic nature of the enzymes or by formation of enzyme-substrate complexes.     

Isolation of bacteriocins through expanded bed adsorption using a hydrophobic interaction medium

Two lactic acid bacterium bacteriocins were isolated from fermentation medium through expanded bed adsorption using a hydrophobic interaction gel. First, amylovorin L471, produced by Lactobacillus amylovorus DCE 471, was selected for the optimisation of the loading and eluting conditions. Secondly, the results of the optimisation were applied for the isolation of enterocin RZS C5, a bacteriocin produced by Enterococcus faecium RZS C5. Optimal adsorption was obtained for a medium with concentration of 1.0 M ammonium sulphate and adjusted to pH 4.0 (94.9% for amylovorin L471 and 75.0% for enterocin RZS C5). Elution with 50% ethanol, buffered at pH 6.0, resulted in an optimal total recovery of the bacteriocin activity of 47.6 and 57.6%, respectively. The highest fold purification expressed as the increase in specific activity (AU/mg) corresponded to the highest recovery, being 140- and 1677-fold, respectively. Nevertheless, a total recovery of only 25.6% with an increase of the specific activity of 121 times was obtained after conventional isolation by ammonium sulphate precipitation.     

New procedure for concentration and analytical isoelectric focusing of proteins.

Proteins in aqueous salt solutions (up to 4 mil) were adsorbed by hydrophobic interaction on phenyl-Sepharose gel (0.1 ml) in small columns. After washing out excess salt, gels were applied on the surface of flat bed polyacrylamide gels for isoelectric focusing, which resulted in efficient desorption and transport of protein out of the phenyl-Sepharose gel. There was no difficulty in obtaining a fifty-fold concentration. The following parameters at adsorption of protein were studied: (i) salt concentration in the protein solution; (ii) phenyl-Sepharose gel adsorptive capacity for protein; (iii) suitable volume of washing solution for the phenyl-Sepharose gel. Theoretical aspects on factors promoting adsorption and desorption of proteins on phenyl-Sepharose gel are discussed. Also discussed are earlier used procedures for concentration and/or dialysis. When dilute protein solutions are to be examined for analytical purposes, the proposed procedures seems to be a valuable aid, which does not require expensive equipment, and is quick and simple to perform.     

Thiophilic adsorption of immunoglobulins--analysis of conditions optimal for selective immobilization and purification

Immunoglobulins have been selected by their general affinity for adjacent sulfone-thioether sulfur groups as a useful model system for the characterization of thiophilic interaction chromatography. Mercaptoethanol coupled to divinylsulfone-activated agarose (thiophilic or T-gel) provided an affinity matrix for the efficient and reversible immobilization of the immunoglobulins. The adsorption/desorption process was investigated as a function of protein concentration, temperature, flow rate, and pH in different concentrations of ammonium sulfate. Immobilization of these proteins was (as a function of pH) found to be both dependent and independent of the adsorption-promoting effects of water-structure-forming salts. Buffer conditions are recommended for the selective adsorption of immunoglobulins from unfractionated human serum. These results indicate that thiophilic interaction chromatography provides a new and effective alternative for the immobilization and purification of immunoglobulins and other proteins under conditions known to preserve structure and biological activity.     

Partial purification of human liver cytochrome P 450.

Human liver cytochrome P 450 was partially purified by hydrophobic chromatography on Octyl-Sepharose, followed by ion-exchange chromatography on DEAE-cellulose. Two fractions (A and B) were obtained; cytochrome P 450 of fraction A was purified sixfold, with an overall yield of about 6 %. Its spectral properties were similar to those previously described in animal cytochromes P 450. Moreover, p-nitroanisole-O-demethylase activity could be obtained in a reconstituted system involving cytochrome P 450 of fraction A, human NADPH-cytochrome $\text{c}$ reductase and phospholipids.     

Adsorption of HSA, IgG and laminin-1 on model titania surfaces--effects of glow discharge treatment on competitively adsorbed film composition

This study investigated the effect of glow discharge treatment of titania surfaces on plasma protein adsorption, by means of ellipsometry and mechanically assisted SDS elution. The adsorption and film elution of three plasma proteins, viz. human serum albumin (HSA), human immunoglobulin G (IgG) and laminin-1, as well as competitive adsorption from a mixture of the three proteins, showed that the adsorbed amount of the individual proteins after 1 h increased in the order HSA 相似文献   

Salt-independent binding of antibodies from human serum to thiophilic heterocyclic ligands

Several thiophilic adsorbents with mercaptoheterocyclic ligands have been analyzed for their ability to bind human serum proteins in a salt-independent way. In contrast to 2-mercaptopyrimidine, 2-mercaptopyridine derived ligands show a group-selective binding of immunoglobulins and α₂-macroglobulin, not only in the presence of high concentrations of sodium sulphate but in buffers with low ionic strength. The binding is restricted to thiophilic gels obtained by coupling 2-mercaptopyridine to a vinylsulphone-activated matrix and is not achieved on epichlorohydrin-activated gels. A novel thiophilic ligand based on mercaptonicotinic acid, containing a carboxylic group together with the thiophilic pattern of thioaromatic adsorbents, is demonstrated to be useful as an alternative purification scheme for antibodies.     

Covalent chromatography and salt-promoted thiophilic adsorption

Covalent chromatography on 3-(2-pyridyl disulfido)-2-hydroxypropyl agarose, abbreviated PyS2, turns out to involve more complex interactions than has been supposed heretofore. Unexpectedly, the sorption is highly salt dependent. The relative affinities for serum proteins have therefore been determined in the absence and presence of different types of salts at different salt concentrations and with different degrees of ligand substitution on the adsorbent. In the presence of water-structuring salts the PyS2-gel shows an adsorption pattern for serum proteins resembling that of the "thiophilic" T-gel (J. Porath; F. Maisano, and M. Belew (1985) FEBS Lett. 185, 306-310). Superimposed on thiophilic adsorption we have found, as expected, covalent attachment of thiol-containing proteins. Also the thiol-disulfide exchange increases from 4-5% in the absence of potassium sulfate or sodium chloride up to about 40% of the applied serum proteins when such a water-structuring salt is present. We have thus shown that the interaction of a protein with the ligand is greatly facilitated by a water-structuring salt--and in this case the product is a covalently as well as a thiophilically immobilized protein. A cautious interpretation of protein interaction phenomena is justified whenever ligands containing sulfide, disulfide, or pi-electron-rich structures such as aromatic moieties are involved.     

Purification of equine IgG using membrane based enhanced hybrid bioseparation technique: a potential method for manufacturing hyperimmune antibody

Hyperimmune equine IgG is widely used as antivenom and anti-rabies agents. This article discusses a membrane based enhanced hybrid bioseparation technique for efficient and scalable purification of equine immunoglobulin G (IgG) from horse serum. This technique is an improved version of a standard hybrid bioseparation technique developed within our group earlier for fractionation of human plasma proteins (Ghosh. 2004. J Membr Sci 237: 109-117). In the presence of a high antichaotropic salt concentration, equine IgG is selectively and reversibly captured within a stirred cell membrane module from horse serum, partly due to precipitation and microfiltration, and partly due to hydrophobic interaction based membrane adsorption, while the impurities are washed out from the device. The reversibly sequestered IgG is then released by lowering the salt concentration which favor both dissolution of the precipitated IgG and desorption of the membrane bound IgG. The enhanced hybrid bioseparation technique improves the IgG recovery from the membrane module by switching from a stirring to non-stirring mode during the IgG release phase. It also reduces membrane fouling by an appropriate pH switch. The effects of operating conditions on equine IgG capture were first systematically studied. The enhanced hybrid bioseparation technique was followed by an ultrafiltration step to remove ammonium sulfate and low molecular weight impurities. The equine IgG purity obtained under optimized conditions was 88% and its recovery was over 90%, both being significantly higher than corresponding values obtained using currently used purification techniques.     

Immobilization of proteins by reductive alkylation with hydrophobic aldehydes

A new method is described for the immobilization of enzymes and other proteins onto hydrophobic gels. Trypsin, for example, can be quantitatively immobilized by reaction with sodium cyanoborohydride and dodecyladehyde-coated Octyl-Sepharose. Noncovalent interactions between the hydrophobic gel and approximately 10 resulting dodecylamino groups in the modified enzyme bind it very strongly but do not affect its ability to hydrolyze benzolarginine ethyl ester. The same procedure can also be used to immobilize E. Coli asparaginase and yeast alcohol dehydrogenase in high yield.     

Butyl-Toyopearl 650 as a new hydrophobic adsorbent for water-soluble enzyme proteins

Butyl-Toyopearl 650, a butyl derivative of Toyopearl HW-65, was synthesized for use in hydrophobic chromatography. Water-soluble enzyme proteins were adsorbed on butyl-Toyopearl 650 in the presence of ammonium sulfate and eluted easily in the absence of the salt. Cytochrome c, myoglobin, and chymotrypsinogen A were successfully separated on a butyl-Toyopearl 650 column in order of their individual hydrophobicity by decreasing the concentration of ammonium sulfate contained in the buffer eluant. Based on these results, the use of butyl-Toyopearl 650 is demonstrated for the hydrophobic separation of water-soluble enzyme proteins.     

Method for the isolation of biologically active monomeric immunoglobulin A from a plasma fraction

A purification method for immunoglobulin A (IgA) yielding monomeric IgA with a purity of over 97% has been developed. This procedure uses ethanol-precipitated plasma (Cohn fraction III precipitate) as the starting material and includes heparin-Sepharose adsorption, dextran sulfate and ammonium sulfate precipitation, hydroxyapatite chromatography, batch adsorption by an anion-exchange matrix and gel permeation. Additional protein G Sepharose treatment leads to an IgA preparation of greater than 99% purity. The isolated IgA presented with an IgA subclass distribution, equivalent to IgA in unfractionated plasma, and was biologically active, as was shown by its ability to down-modulate Haemophilus influenzae-b-induced IL-6 secretion of human monocytes.