Recovery of native protein from potato root water by expanded bed adsorption with amberlite XAD7HP

Potato root water (PRW) contains ～1.5% protein. In this study, expanded bed adsorption (EBA) chromatography with Amberlite XAD7HP resin adsorbent was used to isolate native protein from crude PRW. The optimal pH and ionic strength for potato protein binding onto Amberlite XAD7HP were 5.0 and 20 mmol/L. The EBA-refined proteins were dried by vacuum freeze drying and spray drying at varying outlet temperatures. Results indicated that low temperature spray drying was the most cost effective method with respect to retaining protease inhibitor activities. The dried protein concentrates appeared bright yellow or dark reddish brown, with a total glycoalkaloid content of ～170 μg/g. The protease inhibitor activity was ～400 mg/g and 11 ～ 12 mg/g for trypsin inhibition and chymotrypsin inhibition, respectively. The results presented here suggest that EBA using Amberlite XAD7HP as the adsorbent is a feasible strategy for the direct adsorption of native protein from crude PRW.     

Affinity chromatography of trypsin and related enzymes. V. Basic studies of quantitative affinity chromatography.

A detailed study of the quantitative affinity chromatography of trypsin [EC 3.4.21.4] is reported here. Frontal chromatography using an enzyme solution of very low concentration on an affinity adsorbent gave the dissociation constant of the enzyme-immobilized ligand complex (Kd). Kd values determined under various conditions enabled us to discuss in detail the interaction of trypsin and affinity adsorbents (mainly Gly-Gly-Arg Sepharose). The pH dependence of Kd was consistent with that of the interaction of trypsin and product-type compounds. The effects of changes in temperature, ionic strength, dielectric constant, etc., were also studied. The Ki values of soluble competitive inhibitors can be determined by analysis of their effects on the elution volume of the enzyme. The values obtained were in good agreement with those obtained by kinetic analysis. The present method proved to be useful as a general procedure to investigate the interaction of a protein and a specific ligand.     

Ion exchange chromatography of proteins-prediction of elution curves and operating conditions. I. Theoretical considerations

A mathematical model is proposed for the elution of proteins on ion exchange columns by a linear gradient increase and stepwise increase of ionic strength in order to predict relationships between the elution characteristics (the peak position, the peak width, etc.) and the operating conditions (the flow rate, the slope of gradient, etc). This model is in principle based on the continuous-flow plate theory, in which the protein concentration and ionic strength dependent distibution coefficient between proteins and ion exchangers and zone sperading effects are taken into consideration. The advantage of this model is its simplicity since it requires only two parameters: The distribution coefficient and the number of plates. Since the distribution coefficient of proteins depends on both the protein concentration and ionic strength of the elution buffer, the number of plates should vary with time. However, it is extremely difficult to take into consideration the time-dependent number of plates. Therefore, we assume that the number of plates is constant and related to that number derived from a mass balance model which includes longitudinal dispersion and gel phase diffusion. On the basis of these assumptions, a method for determining the number of plates by the moment method is presented. Although the dependencies of the peak position and peak width on the slope of linear gradient are predictable by numerical calculations of the present model, simpler methods for prediction of these dependencies are desirable. A graphical method is proposed for prediction of the peak position. For prediction of the peak width, an asymptotic solution is derived from a quasi-steady-state model.     

Affinity chromatography of bovine trypsin. A rapid separation of bovine α- and β-trypsin

Affinity adsorbents for bovine trypsin were prepared by covalently coupling p-(p′-amino-phenoxypropoxy)benzamidine to cellulose and to agarose. Trypsin binds to both adsorbents at pH6–8 and is released at low pH values or in the presence of n-butylamine hydrochloride. Pure β-trypsin may be eluted from crude trypsin bound at pH8.0 to the cellulose adsorbent by stepwise elution with an acetate buffer, pH5.0. Both α- and β-trypsin may be isolated by chromatography of crude trypsin on the agarose derivative in an acetate buffer, pH4.0. These two methods for purifying the trypsin are specific to the particular adsorbents. They are rapid and convenient in use. Both methods leave a mixture of the two enzymes bound to the adsorbent and release occurs only at low pH values. The effects of pH, composition and ionic strength of buffer and other variables on both purification methods are described. Affinity adsorbents of soya-bean trypsin inhibitor and of N-α-(N′-methyl-N′-sulphanilyl) sulphanilylagmatine bound to agarose were prepared, but were found to be of limited usefulness in the purification of trypsin.     

Affinity chromatography of Nicotiana tabacum ribonucleases

The purification of tobacco ribonuclease by affinity chromatography is described. 5′-(4-amino-phenylphosphoryl)-guanosine 2′, (3′) phosphate, a ribonuelease inhibitor, has been synthesized and insolubilized onto agarose beads. The resulting adsorbent binds tobacco and some other plant ribonucleases strongly but reversibly at pH 5.4. The bound enzyme can be eluted by changing the pH or ionic strength of the eluting buffer, or by specific elution with substrate or inhibitor. Binding is not due to simple ion-exchange properties of the adsorbent.     

Purification of recombinant enhanced green fluorescent protein expressed in Escherichia coli with new immobilized metal ion affinity magnetic absorbents

A new immobilized metal ion affinity (IMA) adsorbent containing superparamagnetic nanoparticles and coated with hydrophilic resins are proposed here to improve the purification of His-tagged proteins. The magnetic chelating resin was prepared by radical polymerization of magnetite (Fe3O4), styrene, divinyl benzene (DVB) and glycidyl methacrylate-iminodiacetic acid (GMA-IDA) in ethanol/water medium. IDA is immobilized on magnetite as a ligand and pre-charged Cu2+, Zn2+ and Ni2+ as metal ions. To identify the GMA-IDA magnetic particles easily, we named these particles MPGI. The MPGI adsorbent was used to test their suitability for the direct recovery of an intracellular, polyhistidine-tagged protein, enhanced green fluorescent protein [EGFP-(His)(6)], from Escherichia coli lysates in a single step. Parameters influencing the purification efficiencies such as pH, ionic strength and imidazole concentration were optimized to achieve improved separation. The optimal selectively was observed in binding buffer (0.2M NaCl, 0.02M imidazole), washing buffer (0.4M NaCl, 0.03 M imidazole) and elution buffer (0.50M imidazole). The Cu2+-charged MPGI adsorbent had the highest yield and purification factor at 70.4% and 12.3, respectively. The calculated isotherm parameters (Q(m)=53.5 mg/g, K(d)=5.84 mg/mL and Q(m)/K(d)=9.2 mL/g) indicated that the MPGI adsorbent could be used as a suitable adsorbent for EGFP from an aqueous solution.     

Isolation of human urinary protease inhibitor by single-step affinity chromatography.

Human urinary protease inhibitor was isolated from freshly collected male urine by a single chromatographic step utilizing bovine α-chymotrypsin (EC 3.4.21.1) covalently bound to cross-linked agarose. The adsorbent was prepared by a new series of chemical reactions using trichloro-s-triazine as coupler. Study of chromatographic parameters, including pH, temperature, and ionic strength, led to a simplified elution system for removing contaminants. The antitryptic-antichymotryptic activity of the inhibitor appeared to be unaltered by chromatography.     

Development of a mixed mode adsorption process for the direct product sequestration of an extracellular protease from microbial batch cultures

Direct product sequestration of extracellular proteins from microbial batch cultures can be achieved by continuous or intermittent broth recycle through an external extractive loop. Here, we describe the development of a fluidisable, mixed mode adsorbent, designed to tolerate increasing ionic strength (synonymous with extended productive batch cultures). This facilitated operations for the integrated recovery of an extracellular acid protease from cultures of Yarrowia lipolytica. Mixed mode adsorbents were prepared using chemistries containing hydrophobic and ionic groups. Matrix hydrophobicity and titration ranges were matched to the requirements of integrated protease adsorption. A single expanded bed was able to service the productive phase of growth without recourse to the pH adjustment of the broth previously required for ion exchange adsorption. This resulted in increased yields of product, accompanied by further increases in enzyme specific activity. A step change from pH 4.5 to 2.6, across the isoelectric point of the protease, enabled high resolution fixed bed elution induced by electrostatic repulsion. The generic application of mixed mode chemistries, which combine the physical robustness of ion-exchange ligands in sanitisation and sterilisation procedures with a selectivity, which approaches that of affinity interactions, is discussed.     

Effect of glycerol on the interactions and solubility of bovine pancreatic trypsin inhibitor

The effects of additives used to stabilize protein structure during crystallization on protein solution phase behavior are poorly understood. Here we investigate the effect of glycerol and ionic strength on the solubility and strength of interactions of the bovine pancreatic trypsin inhibitor. These two variables are found to have opposite effects on the intermolecular forces; attractions increase with [NaCl], whereas repulsions increase with glycerol concentration. These changes are mirrored in bovine pancreatic trypsin inhibitor solubility where the typical salting out behavior for NaCl is observed with higher solubility found in buffers containing glycerol. The increased repulsions induced by glycerol can be explained by a number of possible mechanisms, all of which require small changes in the protein or the solvent in its immediate vicinity. Bovine pancreatic trypsin inhibitor follows the same general phase behavior as other globular macromolecules where a robust correlation between protein solution second virial coefficient and solubility has been developed. This study extends previous reports of this correlation to solution conditions involving nonelectrolyte additives.     

Complete phenylthiohydantoin amino acid analysis by high-performance liquid chromatography on ULTRASPHERE-octadecyltrimethyloxysllane

All 25 phenylthiohydantoin amino acids have been separated by high-performance liquid chromatography on ULTRASPHERE-octadecyltrimethyloxysilane employing an acetate buffer (pH 5), acetonitrile gradient. The selectivity of the basic and acidic residues can be controlled by manipulation of pH and ionic strength of the mobile phase to optimize resolution between peaks.     

Surface-enhanced laser desorption-ionization retentate chromatography mass spectrometry (SELDI-RC-MS): a new method for rapid development of process chromatography conditions

Protein biochip arrays carrying functional groups typical of those employed for chromatographic sorbents have been developed. When components of a protein mixture are deposited upon an array's functionalized surface, an interaction occurs between the array's surface and solubilized proteins, resulting in adsorption of certain species. The application of gradient wash conditions to the surface of these arrays produces a step-wise elution of retained compounds akin to that accomplished while utilizing columns for liquid chromatography (LC) separations. In retentate chromatography-mass spectrometry (RC-MS), the "retentate" components that remain following a wash are desorbed and ionized when a nitrogen laser is fired at discrete spots on the array after treatment with a laser energy-absorbing matrix solution. Ionized components are analyzed using a time-of-flight mass spectrometer (TOF MS). The present study demonstrates that protein biochips can be used to identify conditions of pH and ionic strength that support selective retention-elution of target proteins and impurity components from ion-exchange surfaces. Such conditions give corresponding behavior when using process-compatible chromatographic sorbents under elution chromatography conditions. The RC-MS principle was applied to the separation of an Fab antibody fragment expressed in Escherichia coli as well as to the separation of recombinant endostatin as expressed in supernatant of Pichia pastoris cultures. Determined optimal array binding and elution conditions in terms of ionic strength and pH were directly applied to regular chromatographic columns in step-wise elution mode. Analysis of collected LC fractions showed favorable correlation to results predicted by the RC-MS method.     

Effect of the nature of proteins on their coupling to different epoxide-containing supports

Quantities of serum albumin, papain, chymotrypsin, trypsin and polyvalent natural trypsin inhibitor antilysin coupled to 3-(2′,3′-epoxypropoxy)propyl-glass, 3-(2′,3′-epoxypropoxy)propyl-silica, epoxyactivated Sepharose 6B, glycidyl methacrylate copolymer and oxirane-acrylic beads (Röhm Pharma) were determined as a function of pH of the reaction mixture. Optimal coupling pH and the amounts of attached individual proteins were considerably affected by both the nature of the coupled protein and the nature of the solid matrix. In some cases the effect of increased ionic strength was studied. Differences in plots of the dependence of the amount of the coupled protein on pH and ionic strength are discussed in respect to the differences of isoelectric points, hydrophobicity and charge distribution of proteins and supports.     

Evaluation of differences between dual salt‐pH gradient elution and mono gradient elution using a thermodynamic model: Simultaneous separation of six monoclonal antibody charge and size variants on preparative‐scale ion exchange chromatographic resin

The efficiencies of mono gradient elution and dual salt‐pH gradient elution for separation of six mAb charge and size variants on a preparative‐scale ion exchange chromatographic resin are compared in this study. Results showed that opposite dual salt‐pH gradient elution with increasing pH gradient and simultaneously decreasing salt gradient is best suited for the separation of these mAb charge and size variants on Eshmuno^® CPX. Besides giving high binding capacity, this type of opposite dual salt‐pH gradient also provides better resolved mAb variant peaks and lower conductivity in the elution pools compared to single pH or salt gradients. To have a mechanistic understanding of the differences in mAb variants retention behaviors of mono pH gradient, parallel dual salt‐pH gradient, and opposite dual salt‐pH gradient, a linear gradient elution model was used. After determining the model parameters using the linear gradient elution model, 2D plots were used to show the pH and salt dependencies of the reciprocals of distribution coefficient, equilibrium constant, and effective ionic capacity of the mAb variants in these gradient elution systems. Comparison of the 2D plots indicated that the advantage of opposite dual salt‐pH gradient system with increasing pH gradient and simultaneously decreasing salt gradient is the noncontinuous increased acceleration of protein migration. Furthermore, the fitted model parameters can be used for the prediction and optimization of mAb variants separation in dual salt‐pH gradient and step elution. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:973–986, 2018     

Effect of solution pH and ionic strength on the separation of albumin from immunoglobulins (IgG) by selective filtration

Although protein fractionation by selective membrane filtration has numerous potential applications in both the downstream processing of fermentation broths and the purification of plasma proteins, the selectivity for proteins with only moderately different molecular weights has generally been quite poor. We have obtained experimental data for the transport of bovine serum albumin (BSA) and immunoglobulins (IgG) through 100,000 and 300,000 molecular weight cutoff polyethersulfone membranes in a stirred ultrafiltration device at different solution pH and ionic strength. The selectivity was a complex function of the flux due to the simultaneous convective and diffusive solute transport through the membrane and the bulk mass transfer limitations in the stirred cell. Under phsioligical conditions (pH 7.0 and 0.15 M NaCI) the maximum selectivity for the BSA-IgG separation was only about 2.0 due primarily to the effects of protein adsorption. In contrast, BSA-IgG selectivities as high as 50 were obtained with the same membranes when the protein solution was at pH 4.8 and 0.0015 M NaCl. This enhanced selectivity was a direct result of the electrosatatic contributions to both bulk and membrane transport. The membrane selectivity could actually be reversed, with higher passage of the larger IgG molecules, by using a 300,000 molecular weight cutoff membrane at pH 7.4 and an ionic strength of 0.0015 M NaCl. These results clearly demonstrate that the effectiveness of selective protein filtration can be dramatically altered by appropriately controlling electrostatic interactions through changes in pH and/or ionic strength. (c) 1994 John Wiley & Sons, Inc.     

Comparison of the binding behavior of several histidine-containing proteins with immobilized copper(II) complexes of 1,4,7-triazacyclononane and 1,4-bis(1,4,7-triazacyclononan-1-yl)butane

The protein binding characteristics of the immobilized binucleating chelate system, 1,4-bis(1,4,7-triazacyclononan-1-yl)butane (tacn(2)butane), complexed with Cu(2+) ions have been investigated with hen egg white lysozyme, horse skeletal muscle myoglobin and horse heart cytochrome C, as well as three histidine-rich proteins, serum albumin, transferrin, and α(2)-macroglobulin, present in partially fractionated human serum. The effects of pH, ionic strength and elution buffers on protein binding have been examined and compared with those of the analogous immobilized mononuclear copper complex of 1,4,7-triazacyclononane (tacn). The Cu(2+)-tacn(2)butane system was generally found to exhibit higher protein binding affinities than the Cu(2+)-tacn system, suggesting that the presence of immobilized binuclear copper(II) species leads to enhanced coordinative interaction with surface-exposed amino acid residues of the studied proteins. However, under some buffer conditions the dependencies of protein binding and elution on pH and ionic strength with these immobilized metal ion affinity chromatographic (IMAC) systems were consistent with electrostatic, hydrophobic and π-bonding interactions playing a significant secondary role in addition to the dominant coordinative interactions. As such, the results indicated that the selectivities were not solely dependent on the histidine content of the protein. In accord with this conclusion, differences in the selectivities of the Cu(2+)-tacn and Cu(2+)-tacn(2)butane adsorbents for serum albumin, transferrin, and α(2)-macroglobulin were observed depending on the choice of elution buffer. This attribute suggests that additional selectivity features can be realised for the separation of specific proteins with this new class of adsorbent.     

Selection of monoclonal antibodies for immunoaffinity chromatography: model studies with antibodies against soy bean trypsin inhibitor

To facilitate selection of monoclonal antibodies for immunoaffinity chromatography, an ELISA screening procedure was developed. The assay is based on the avidin-biotin system and provides a profile of the monoclonal antibody which is based on the binding characteristics of the antigen binding site when exposed to different elution reagents. The elution profiles of 5 monoclonal antibodies to soy bean trypsin inhibitor (SBTI) were determined and for 2 of the antibodies the results obtained in the ELISA were verified using column experiments. The affinity constants were determined for the same 5 monoclonal antibodies and no correlation was seen with the ease of elution. The elution profiles presented here are easily obtained and the results indicate that a general screening procedure for suitable combinations of antibodies and elution conditions can be carried out using an elution ELISA assay when modified as described herein.     

One-step chromatography method for efficient separation and purification of R-phycoerythrin from Polysiphonia urceolata

Phycoerythrins have been widely used in food, cosmetics, immunodiagnostics and analytical reagents. An efficient one-step chromatography method for purification of R-phycoerythrins from Polysiphonia urceolata was described in this paper. Pure R-phycoerythrin was obtained with an absorbance ratio A(565)/A(280) of 5.6 and a high recovery yield of 67.33% using a DEAE-Sepharose Fast Flow chromatography with a gradient elution of pH, alternative to common gradient elution of ionic strength. The absorption spectrum of R-phycoerythrin was characterized with three absorbance maxima at 565, 539 and 498 nm, respectively and the fluorescence emission spectrum at room temperature was measured to be 580 nm. The results of native-PAGE, and SDS-PAGE showed no contamination by other proteins in the phycoerythrin solution, which suggests an efficient method for the separation and purification of R-phycoerythrins from Polysiphonia urceolata.     

Neuropeptide processing activity in Aplysia bag cell homogenates

The neurosecretory bag cells of the mollusk, Aplysia, generate a peptide egg-laying hormone (ELH) from a 29,000 Dalton precursor protein by proteolytic cleavage to a 6-9,000 Dalton intermediate, followed by cleavage of the intermediate. We report here the initial characterization of these cleavage activities. Homogenates of bag cells in low ionic strength buffer process endogenous precursor to a peptide which is indistinguishable from ELH in molecular weight and isoelectric point. Non-specific proteolysis in the homogenates is not detectable. The pH optimum for cleavage of the precursor and the intermediate is 5.5-6.5. The cleavage activities exhibit a substantial degree of membrane association, and the inhibitor profile of each is characteristic of a thiol protease without a metal cofactor requirement. Precursor cleavage activity differs from that of the intermediate cleaving activity in inhibitor profile, solubility, and slightly, in pH optimum.     

Dynamic electric field assisted multi-dimensional liquid chromatography of biological samples

Complex biological samples require very high resolution separation strategies. The platform introduced here capitalises on the hyphenation of liquid chromatographic (LC) and electric potential gradient electrochromatographic multi-dimensional separation genres. First-dimension selectivity is provided by simultaneous size exclusion (SEC) and strong cation exchange (SCX) chromatography modes, while the second dimension comprises reversed phase (RP) characteristics in a dynamic (time-variant) electric field. The time-variant potential gradient with reversal of polarity is applied across the second dimension monolithic capillary throughout the duration of the solvent strength gradient elution. Hence, the platform offers comprehensive on-line sample clean-up (matrix depletion, analyte enrichment), fractionation (first dimention LC), and separation (second dimension LC) with the prospect of altering selectivity via polarity reversal dynamic electric field tuning.     

Recovery of aprotinin from insulin industrial process effluent by affinity adsorption

Aprotinin is a protease inhibitor found in bovine organs and used as a valuable human therapeutic compound. In this work, a process for the recovery of aprotinin from insulin industrial process effluent via affinity adsorption on immobilized trypsin and chymotrypsin was developed. First, process conditions were set as a result of a study of the effects of pH and ionic strength on pure aprotinin adsorption and desorption utilizing an experimental design methodology. The best conditions obtained with immobilized trypsin as the ligand were adsorption at 0.018 M NaCl and pH 8.7 and desorption at 0.018 M NaCl and pH 2.1. For immobilized chymotrypsin, the best conditions were adsorption at 0.582 M NaCl and pH 8.0 and desorption at 0.582 M NaCl and pH 2.1. Recovery of the inhibitor from the effluent was carried out utilizing a two-step process: trypsin-agarose adsorption followed by chymotrypsin-agarose adsorption. Analysis of the chromatographic fractions by trypsin and chymotrypsin inhibition and capillary electrophoresis assays strongly suggested that the recovered inhibitor is aprotinin.