Plate height determination for gradient elution chromatography of proteins

A method for determining the plate height HETP from the elution curve obtained by the linear gradient elution (LGE) ion-exchange chromatography (IEC) of proteins is presented. The method was developed on the basis of the numerical solutions of a chromatography model which considers the zone sharpening and the distribution coefficient as a function of the salt concentration. The plate height HETP is determined from the peak width and the salt concentration at which the peak is eluted in LGE. The method was applied to the experimental results with various ion-exchange chromatography media. A calculation example based onthe present method is presented to show how the chromatographic and operating parameters should be tuned to obtain a desired resolution. A simplified calculation procedure for the peak profile is also described. (c) 1995 John Wiley & Sons, Inc.     

Salt-tolerant cation exchanger-containing sulfate groups as a viable alternative for mixed-mode type and heparin-based affinity resins

Ion-exchange chromatography is still one of the most popular protein separation techniques. Before chromatographic separation, the high salt concentration in various samples necessitates additional steps. Therefore, low salt tolerance of ion-exchange resins is a drawback that needs to be addressed. Herein, the differences in salt tolerance and hydrophobicity of strong cation-exchange TOYOPEARL resins of sulfonium and sulfate-types were investigated. Despite only a minor structural difference, differences in selectivity and salt tolerance between the sulfate and sulfonic groups were detected. In silico calculations were also carried out for model substances representing the sulfonium and sulfate groups, wherein significant differences in hydrophobicity was observed. These experiments confirmed the hypothesis that the salt tolerance, higher affinity, and selectivity for certain vitamin K dependent clotting factors are interrelated and dependent on the presence of the sulfate group. Separation of clotting factor IX from the prothrombin complex concentrate further to confirmed the affinity for these proteins. The results show that the use of only a resin with the sulfate ligand and not with the sulfonic acid ligand allows for a facile and rapid separation of clotting factor IX and other vitamin K dependent clotting factors.     

Identification of the mass transfer mechanisms involved in the transport of human immunoglobulin-G in N,N,N',N'-ethylenediaminetetramethylenephosphonic acid-modified zirconia

Zirconia particles modified with N,N,N',N'-ethylenediaminetetramethylenephosphonic acid (EDTPA), further referred to as r_PEZ, were studied as a support material for use in chromatography. Our previous studies have demonstrated the utility of r_PEZ in the separation of immunoglobulins from biological fluids. In the present study we sought to understand the underlying factors and identify the rate-limiting mechanisms that govern the transport of biomolecules in r_PEZ. Pulse injection techniques were used to elucidate the individual mass transfer parameters. Elution profiles obtained under retained and unretained conditions were approximated by the Gaussian equation and the corresponding HETP contributions were estimated. The dependence of the HETP values on incremental salt concentration in the mobile phase was determined. Resulting data in conjunction with the equations outlined in literature were used to estimate the theoretical number of transfer units for the chromatographic separation process. Our results indicate that surface diffusion probably plays a minor role; however pore diffusion was established to be the rate limiting mechanism for immunoglobulin G adsorption to r_PEZ. The HETP based methodology may be used to estimate the rate limiting mechanisms of mass transfer for any given chromatographic system under appropriate conditions.     

Protein instability during HIC: describing the effects of mobile phase conditions on instability and chromatographic retention

Hydrophobic interaction chromatography (HIC) is known to be potentially denaturing to proteins, but the effects of mobile phase conditions on chromatographic behavior are not well understood. In this study, we apply a model describing the effects of secondary protein unfolding equilibrium on chromatographic behavior, including the effects of salt concentration on both stability and adsorption. We use alpha-lactalbumin as a model protein that in the presence and absence of calcium, allows evaluation of adsorption parameters for folded and unfolded species independently. The HIC adsorption equilibrium under linear binding conditions and solution phase protein stability have been obtained from a combination of literature and new experiments. The effect of salt concentration on protein stability and the rate constant for unfolding on the chromatographic surface have been determined by fitting the model to isocratic chromatography data under marginally stable conditions. The model successfully describes the effects of added calcium and ammonium sulfate. The results demonstrate the importance of considering the effects on stability of mobile phase modifiers when applying HIC to marginally stable     

High-throughput screening of chromatographic separations: II. Hydrophobic interaction

A high-throughput screen (HTS) was developed to evaluate the selectivity of various hydrophobic interaction chromatography (HIC) resins for separating a mAb from aggregate species. Prior to the resin screen, the solubility of the protein was assessed to determine the allowable HIC operating region by examining 384 combinations of pH, salt, and protein concentration. The resin screen then incorporated 480 batch-binding and elution conditions with eight HIC resins in combination with six salts. The results from the screen were reproducible, and demonstrated quantitative recovery of the mAb and aggregate. The translation of the HTS batch-binding data to lab-scale chromatography columns was tested for four conditions spanning the range of product binding and selectivity. After accounting for the higher number of theoretical plates in the columns, the purity and recovery of the lab-scale column runs agreed with the HTS results demonstrating the predictive power of the filterplate system. The HTS data were further analyzed by the calculation of pertinent thermodynamic parameters such as the partition coefficient, K(P), and the separation factor, alpha. The separation factor was used to rank the purification capabilities of the resin and salt conditions explored.     

Extension of the selection of protein chromatography and the rate model to affinity chromatography

The rational selection of optimal protein purification sequences, as well as mathematical models that simulate and allow optimization of chromatographic protein purification processes have been developed for purification procedures such as ion-exchange, hydrophobic interaction and gel filtration chromatography. This paper investigates the extension of such analysis to affinity chromatography both in the selection of chromatographic processes and in the use of the rate model for mathematical modelling and simulation. Two affinity systems were used: Blue Sepharose and Protein A. The extension of the theory developed previously for ion-exchange and HIC chromatography to affinity separations is analyzed in this paper. For the selection of operations two algorithms are used. In the first, the value of η, which corresponds to the efficiency (resolution) of the actual chromatography and, Σ, which determines the amount of a particular contaminant eliminated after each separation step, which determines the purity, have to be determined. It was found that the value of both these parameters is not generic for affinity separations but will depend on the type of affinity system used and will have to be determined on a case by case basis. With Blue Sepharose a salt gradient was used and with Protein A, a pH gradient. Parameters were determined with individual proteins and simulations of the protein mixtures were done. This approach allows investigation of chromatographic protein purification in a holistic manner that includes ion-exchange, HIC, gel filtration and affinity separations for the first time.     

Optimization of step gradient separations: Consideration of nonlinear adsorption

Nonlinear adsorption plays an important role in determining the chromatographic behavior of proteins in preparative ion-exchange chromatography. In this article, the steric mass action (SMA) isotherm is used in conjunction with a mass transport model to describe nonlinear cation-exchange chromatography. Excellent agreement is observed between simulated and experimental step gradient separations of the proteins alpha-chymotryp-sinogen A, cytochrome C, and lysozyme. A systematic method of selecting the optimum step gradient program for a given separation problem is presented and employed to study optimization of step gradient chromatography under conditions of high mass loading. This article includes consideration of the effects of the adsorption properties of the feed stream, the feed stream concentration, protein solubility, and otherconstraints on the optimum separation conditions.(c) John Wiley & Sons, Inc.     

Comparison of linear gradient and displacement separations in ion-exchange systems

The linear gradient mode of chromatography is the most widely employed mode of operation in ion-exchange chromatographic separations. However, in recent years, the displacement mode has received considerable attention because of its promise of high throughput and high resolution. To enable a comparison of these two modes of chromatography, it is essential to identify the optimum operating conditions for each. We employed an iterative algorithm to carry out the necessary optimization. The Steric Mass Action model of ion-exchange chromatography is used in concert with the solid-film linear-driving force model to describe the chromatographic behavior of the solutes in these systems. The performances of displacement and gradient modes of chromatography are compared for different types of separation problems. It turns out that for "easy" separations, both the modes are equally effective. However, for challenging separations, the displacement mode is superior to the gradient mode. Our results shed significant light on the performance of gradient and displacement modes in protein ion-exchange systems.     

Negative chromatography: Progress,applications and future perspectives

In negative chromatography, the impurities bind on the adsorbent, and the product is allowed to flow through the chromatographic column. Negative chromatography is an alternative to positive chromatography under certain circumstances and has been used to purify various biomolecules. For this review, a detailed survey of the performance of reported studies on negative chromatography was conducted. The applications of negative chromatography in the capture and intermediate purification steps for biomolecules (e.g., plasmid DNA, antibodies, enzymes, hemoglobin, virus particles and cells) are reviewed. The negative chromatographic adsorbents adsorb the impurities through surface charge, hydrophobic interaction at specific sites on the surface, hydrophobic interaction, hydrogen bonding and functional groups. Examples of applications of negative chromatography according to the type of chromatography matrix used are summarized and discussed. In addition, the effects of operating conditions (initial protein concentration, buffer ions, pH and salt concentration) are discussed, and the criteria for choosing negative or positive chromatography are summarized. The literature survey showed that there will be future limitations and challenges ahead in implementation of negative chromatography. Possible solutions to the limitations and challenges of negative chromatography and future trends for developing negative chromatography are discussed.     

Separation of proteins by high-speed pressure liquid chromatography

Two chromatographic systems for separation of proteins by high-speed pressure liquid chromatography are described. Molecular size exclusion chromatography was achieved by the use of porous silica deactivated by Carbowax-20M to prevent protein adsorption. Protein separations were successful provided the salt concentration in the eluting buffer was relatively high.The second system described is adsorption chromatography of proteins on deactivated Porasil. This technique involves elution of the proteins from the gel by means of a salt and pH gradient. In both systems the total time required for the chromatography is less than 1 hr.     

Study of the mechanism of interaction of antibody (IgG) on two mixed mode sorbents

Purification of target proteins from a crude biological mixture containing proteins, peptides and other biomolecules is the chromatographic challenge. Mixed mode chromatography offers additional selectivities to improve the overall productivity of commercial bioprocesses with novel chromatographic sorbents being introduced to overcome the problem. HEA HyperCel? (n-hexyl amine) and PPA HyperCel? (phenyl propyl amine) are industry scalable mixed mode chromatography sorbents where both hydrophobic and electrostatic interactions are predominant. Our study focuses on understanding the underlying mechanism of interaction of protein with the sorbent. Parameters like buffer conditions, pH and temperature were tuned to study the adsorption and desorption conditions of the protein. Dynamic binding capacity of HEA HyperCel? and PPA HyperCel? sorbents was studied with human IgG as a model protein. Our study shows that, in HEA the interaction of IgG to the sorbent is predominantly hydrophobic as the binding is enhanced (50–60 mg/ml of sorbent) by presence of salt in buffer and increase in temperature. Binding capacity of PPA is 50–60 mg/ml of sorbent irrespective of temperature effect and/or the presence of salt. The chromatographic experiments show that the interaction could be hydrophobic or ionic or some charge transfer mechanism depending upon the buffer conditions.     

Purification of isopenicillin N synthetase from Streptomyces clavuligerus

Isopenicillin N synthetase was purified from Streptomyces clavuligerus by sequential salt precipitation, ion-exchange and gel-filtration chromatography using both conventional open column and high-performance liquid chromatographic techniques. Material from the final purification step had a specific activity of 204.1 X 10(-3) units/mg of protein which represented a 130-fold purification over the cell-free extract. The purified isopenicillin N synthetase was determined to have a molecular weight of 33,000 by sodium dodecyl sulfate-polyacrylamide gel electrophoresis and to have a Km of 0.32 mM with respect to its substrate delta-(L-alpha-aminoadipyl)-L-cysteinyl-D-valine. The enzyme showed a sensitivity to thiol-specific inhibitors with N-ethylmaleimide giving the strongest inhibitory effect.     

Purification of Escherichia coli alkaline phosphatase on an ion-exchange high-performance liquid chromatographic column using carboxymethyl dextrans

Carboxymethyl dextrans (CM-Ds) were used on an HPLC ion-exchange column to obtain significantly enriched alkaline phosphatase (EC 3.1.3.1) from a sample of Escherichia coli periplasmic space proteins without significant loss of enzymatic activity. The ability of CM-Ds to separate alkaline phosphatase even when the column was 80-85% saturated with protein demonstrates the potential for high column capacity using CM-Ds. In addition, the fractions containing alkaline phosphatase and CM-Ds were reapplied to the same ion-exchange column under different buffer conditions and purified to homogeneity by salt gradient elution chromatography, thus demonstrating the compatibility of CM-Ds with the latter chromatographic method. The two-step chromatographic procedure yielded enzyme of purity comparable to that of electrophoretically purified E. coli alkaline phosphatase obtained commercially. These studies demonstrate that HPLC displacement chromatography is a mild procedure which allows rapid, quantitative purification of an enzyme. Scaling up with larger columns should allow purification of enzymes of a commercial basis.     

Recent development of multi-dimensional chromatography strategies in proteome research

As a complementary approach to two-dimensional polyacrylamide gel electrophoresis (2D-PAGE), multi-dimensional chromatography separation methods have been widely applied in all kinds of biological sample investigations. Multi-dimensional liquid chromatography (MDLC) coupled with bio-mass spectrometry (MS) is playing important roles in proteome research due to its high speed, high resolution and high sensitivity. Proteome analysis strategies mainly include bottom-up and top-down approaches which carry out biological sample separation based on peptide and protein levels, respectively. Electrophoretic methods combined with liquid chromatography like IEF-HPLC and HPLC-SDS-PAGE have been successful applied for protein separations. As for MDLC strategy, ion-exchange chromatography (IEX) together with reversed phase liquid chromatography (RPLC) is still a most widely used chromatography in proteome analysis, other chromatographic methods are also frequently used in protein pre-fractionations, while affinity chromatography is usually adopted for specific functional protein analysis. Recent MDLC technologies and applications to variety of proteome analysis have been achieved great development. A digest peptide-based approach as so-called "bottom-up" and intact protein-based approach "top-down" analysis of proteome samples were briefly reviewed in this paper. The diversity of combinations of different chromatography modes to set up MDLC systems was demonstrated and discussed. Novel developments of MDLC techniques such as high-abundance protein depletion and chromatography array were also included in this review.     

High-throughput process development for recombinant protein purification

Methods development in chromatographic purification processes is a complex operation and has traditionally relied on trial and error approaches. The availability of a large number of commercial media, choice of different modes of chromatography, and diverse operating conditions contribute to the challenging task of accelerating methods development. In this paper, we describe a novel microtiter-plate based screening method to identify the appropriate sequence of chromatographic steps that result in high purities of bioproducts from their respective culture broths. Protein mixtures containing the bioproduct were loaded on aliquots of different chromatographic media in microtiter plates. Serial step elution of the proteins, in concert with bioproduct-specific assays, resulted in the identification of "active fractions" containing the bioproduct. The identification of a successful chromatographic step was based on the purity of the active fractions, which were then pooled and used as starting material for screening the next chromatographic dimension. This procedure was repeated across subsequent dimensions until single band purities of the protein were obtained. The sequence of chromatographic steps and the corresponding operating conditions identified from the screen were validated under scaled-up conditions. Various modes of chromatography including hydrophobic interaction, ion exchange (cation and anion exchange) and hydrophobic charge-induction chromatography (HCIC), and different operating conditions (pH, salt concentration and type, etc.) were employed in the screen. This approach was employed to determine the sequence of chromatographic steps for the purification of recombinant alpha-amylase from its cell-free culture broth. Recommendations from the screen resulted in single-band purity of the protein under scaled-up conditions. Similar results were observed for an scFv-beta-lactamase fusion protein. The use of a miniaturized screen enables the parallel screening of a wide variety of actual bioprocess media and conditions and represents a novel paradigm approach for the high-throughput process development of recombinant proteins.     

High performance liquid chromatography of nucleotides. Major methods and their development

The separation of mono- and oligonucleotides possibilities by means of high performance ion-exchange, reversed-phase, so-called "ion-pair" and adsorption chromatography are studied. The influence of the eluent composition (solvent, salt) and pH on the retention, selectivity and resolution in reversed-phase and ion-exchange chromatography is investigated. The model of the hydrophobic-pair ion-exchange mechanism of ion-pair chromatography is considered. The conditions for analysis and preparative isolation of a desired component are optimized for selectivity, resolution and throughput. The methods for prediction of the optimal gradient elution program reasonable resolution at the desired retention time and for choosing the guard-column packing material are proposed. A design of the gradient for system and the version of slurry packing method for HPLC prolonged life-time columns are improved. The automatized analytical technique for determination of the oligonucleotide monomeric composition with two coupled microcolumns is described, that involves enzymatic digestion of an oligonucleotide followed by ion-exchange separation of the hydrolysate.     

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.     

Polymer displacement/shielding in protein chromatography

An overview of different applications of polymer interactions with ion-exchange and dye-affinity chromatographic matrices is presented here. The strength of interaction between the ligand and the polymer plays a crucial role in deciding the mode of chromatographic application. Charged, non-ionic and thermosensitive polymers such as poly(ethylene imine), poly(N-vinyl pyrrolidone) and poly(vinyl caprolactam) respectively, show different degrees of interaction with the dye molecules in dye ligand chromatography. Polymers, with their ability of multipoint and hence strong attachment to the chromatographic matrices, were used as efficient displacers in displacement chromatography. The polymer displacement resulted in better recoveries and sharper elution profiles than traditional salt elutions. The globule–coil transition of the thermosensitive reversible soluble–insoluble polymer, poly(vinyl caprolactam), can be exploited in dye-affinity columns for the temperature induced displacement of the bound protein. In another situation, prior to the column chromatography of crude protein extract, polymers formed complexes with the dye matrix and “shielded” the column. The polymer shielding decreased the nonspecific interactions without affecting the specific interactions of the target protein to the dye matrix.     

Modelling of the chromatographic separation of xylose-mannose in ion-exchange resin columns

A mathematical model was proposed for the chromatographic separation of xylose and mannose on an ion-exchange resin in the Pb form: dispersion in the mobile phase, external mass transfer around the particles and internal diffusion were taken into account. Small-scale experiments provided an evaluation of the different parameters. Dispersion in the mobile phase was found to be the predominant phenomenon. The Peclet numbers were calculated by identification in the Laplace domain of the elution profiles. Influence of temperature and initial concentration of the sample were studied.     

Rapid chromatofocusing of proteins

Chromatofocusing, a chromatographic technique whereby proteins are selectively eluted from an ion-exchange support according to their pI values, has been adapted to high-performance liquid chromatography. It was found that chromatofocusing can detect heterogeneity in protein preparations not demonstrated by reverse-phase or size exclusion chromatography and that the resolution of chromatofocusing is comparable to ion-exchange chromatography. Although chromatofocusing may not resolve proteins as well as isoelectric focusing, it has advantages over this technique in both speed and capacity. The usefulness of chromatofocusing as an additional technique in the analysis and preparation of proteins is discussed. The rapid separation technique described here is able to resolve protein mixtures in the chromatofocusing mode in approximately 30 min.