Constant-pattern design method for displacement chromatography

Displacement chromatography can be used for the purification of many types of chemicals and biochemicals. In the constant-pattern mode, this method can be used for concentrating and separating various mixtures, leading to higher yields and sorbent productivities than elution chromatography. There are, however, no commercial-scale applications of displacement chromatography. One major barrier is the difficulty in specifying the design variables for reaching a constant-pattern state. A second barrier is that productivity is limited when the feed mixture contains a minority component. In this study, a constant-pattern design method is developed to overcome the first barrier. Theoretical analyses and strategically chosen combinations of key dimensionless groups are used for reducing the multi-dimensional parameter space into a two-dimensional space. Systematic rate model simulations are used to find a general correlation, which divides the two-dimensional space into a transient region and a constant-pattern region. A predictive design method based on the general correlation is developed to find the designs for achieving required product purities and yields with the highest productivities. The design method was shown to increase significantly the productivities or yields for the separations of three binary mixtures. To overcome the second barrier, a multi-zone displacement chromatography method is presented for dividing the separation tasks in multiple zones. For a specific ternary mixture containing a minority component, the sorbent productivity for a two-zone design was 680 times higher than that of a single-column design. This method can be used for developing efficient displacement chromatography processes for purifying a wide range of complex mixtures.

Two Dimensional Anion Exchange-Size Exclusion Chromatography Combined with Mathematical Modeling for Downstream Processing of Foot and Mouth Disease Vaccine

The production of high-quality purified virus particles in high quantities for vaccine preparation requires a scalable purification procedure in the downstream step. A purification scheme based on combined strong anion-exchange and size exclusion chromatography (2D-AEC-SEC) was developed for the production of non-structural protein-free foot and mouth disease vaccine, and the whole procedure was accomplished with 77.9% virus yield. Additionally, a mathematical modeling and a simulation approach based on a plate model of chromatography were developed and matched with the experimental chromatography data to improve prediction of retention behavior and save time in the development of the downstream scale-up method. The purified pooled virus fraction obtained from the final polishing step had a purity higher than 85% based on analytical size exclusion analysis. Moreover, more than 90.1% of residual DNA (rDNA) was removed from the purified vaccine. The analysis of purified virus particles by sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE), dynamic light scattering (DLS), high performance size exclusion chromatography (HP-SEC), matrix-assisted laser desorption/ionization time-of-flight mass spectrometry (MALDI-TOF MS), and transmission electron microscopy (TEM) provided clear evidence of purity and demonstrated that the final product is structurally spherical, intact particles qualified for formulation as a vaccine product.

Displacement to separate host-cell proteins and aggregates in cation-exchange chromatography of monoclonal antibodies

An efficient and consistent method of monoclonal antibody (mAb) purification can improve process productivity and product consistency. Although protein A chromatography removes most host-cell proteins (HCPs), mAb aggregates and the remaining HCPs are challenging to remove in a typical bind-and-elute cation-exchange chromatography (CEX) polishing step. A variant of the bind-and-elute mode is the displacement mode, which allows strongly binding impurities to be preferentially retained and significantly improves resin utilization. Improved resin utilization renders displacement chromatography particularly suitable in continuous chromatography operations. In this study we demonstrate and exploit sample displacement between a mAb and impurities present at low prevalence (0.002%-1.4%) using different multicolumn designs and recycling. Aggregate displacement depends on the residence time, sample concentration, and solution environment, the latter by enhancing the differences between the binding affinities of the product and the impurities. Displacement among the mAb and low-prevalence HCPs resulted in an effectively bimodal-like distribution of HCPs along the length of a multi-column system, with the mAb separating the relatively more basic group of HCPs from those that are more acidic. Our findings demonstrate that displacement of low-prevalence impurities along multiple CEX columns allows for selective separation of mAb aggregates and HCPs that persist through protein A chromatography.

Application of Displacement Chromatography to Online Two-Dimensional Liquid Chromatography Coupled to Tandem Mass Spectrometry Improves Peptide Separation Efficiency and Detectability for the Analysis of Complex Proteomes

The complexity of mammalian proteomes is a challenge in bottom-up proteomics. For a comprehensive proteome analysis, multidimensional separation strategies are necessary. Online two-dimensional liquid chromatography–tandem mass spectrometry (2D-LC-MS/MS) combining strong cation exchange (SCX) in the first dimension with reversed-phase (RP) chromatography in the second dimension provides a powerful approach to analyze complex proteomes. Although the combination of SCX with RP chromatography provides a good orthogonality, only a moderate separation is achieved in the first dimension for peptides with two (+2) or three (+3) positive charges. The aim of this study was to improve the performance of online SCX-RP-MS/MS by applying displacement chromatography to the first separation dimension. Compared to gradient chromatography mode (GCM), displacement chromatography mode (DCM) was expected to improve the separation of +2-peptides and +3-peptides, thus reducing complexity and increasing ionization and detectability. The results show that DCM provided a separation of +2-peptides and +3-peptides in remarkably sharp zones with a low degree of coelution, thus providing fractions with significantly higher purities compared to GCM. In particular, +2-peptides were separated over several fractions, which was not possible to achieve in GCM. The better separation in DCM resulted in a higher reproducibility and significantly higher identification rates for both peptides and proteins including a 2.6-fold increase for +2-peptides. The higher number of identified peptides in DCM resulted in significantly higher protein sequence coverages and a considerably higher number of unique peptides per protein. Compared to conventionally used salt-based GCM, DCM increased the performance of online SCX-RP-MS/MS and enabled comprehensive proteome profiling in the low microgram range.

Csaba Horváth and preparative liquid chromatography

Few chromatographers have been interested in furthering preparative liquid chromatography. The pioneers, Tswett, Kuhn and Lederer, A.J.P. Martin, Tiselius, isolated fractions but as an intermediate step in the analysis of their samples. The progress in electronics and sensors, and in their miniaturization has lead to the paradoxical situation that the analysts never see the transient pure fractions that their detector quantitates. Yet, over the last 25 years, preparative liquid chromatography has become an important industrial process for the separation, the extraction, and/or the purification of many pharmaceuticals or pharmaceutical intermediates, including pure enantiomers, purified peptides and proteins, compounds that are manufactured at the relatively large industrial scale of a few kilograms to several hundred tons per year. This development that has strongly affected the modem pharmaceutical industry is mainly due to the pioneering work of Csaba Horváth. His work in preparative HPLC was critical at both the practical and the theoretical levels. He was the first scientist in modem times to pay serious attention to the relationships between the curvature of the equilibrium isotherms, the competitive nature of nonlinear isotherms, and the chromatographic band profiles of complex mixtures. The thermodynamics of multi-component phase equilibria and mass transfer kinetics in chromatography attracted his interest and were the focus of ground-breaking contributions. He investigated displacement chromatography, an old method invented by Tiselius that Csaba was first to implement in HPLC. This choice was explained by the essential characteristic of displacement chromatography, in that it delivers fractions that can be far more concentrated than the feed. Remarkably, once the basics of nonlinear chromatography had been mastered in his group, most of the applications that were studied by his coworkers dealt with peptides of various sizes and with proteins. Thus, all the applications of preparative HPLC in the biotechnologies derive directly from Csaba's work. Although displacement did not pan out as a general method, the reasons are related more to practical constraints of the production of pharmaceuticals and to the long period of cheap energy that might be ending now. This report reviews Csaba's work in nonlinear chromatography.

The contributions of Csaba Horváth to liquid chromatography

This article is not a biographic description of the life of Csaba Horváth, but an attempt to describe his most important contributions to liquid chromatography, as viewed by an author who himself started with HPLC in 1973. With the introduction of columns packed with rigid pellicular particles, which could withstand high pressures, the combination of fast separations with high efficiency was designated high pressure liquid chromatography about 35 years ago. The contribution of Horváth to the birth of modern LC was to imagine the potential for high-speed separations in LC by transferring ideas and technology from gas chromatography. From this time, his strong participation in understanding and describing the processes of separation science made him a leading scientist in fundamental studies of separation principles until his passing away in April 2004. In addition to being one of the forefathers of modern liquid chromatography, Csaba Horváth described both the ionic interactions and the hydrophobic interactions on ion exchangers as well as on reversed phase materials and developed a theoretical basis for understanding these processes. If one person should be mentioned as the inventor of ion-pair chromatography of organic compounds, of hydrophobic interaction chromatography, and of the theoretical basis for reversed phase chromatography, this person is Csaba Horváth. Throughout the last 30 years he also had a strong interest in studying proteins in separation processes, and in the last decade he made valuable contributions to capillary electrochromatography, particularly for separation of proteins on monolithic columns. For this author is difficult to find another person who has had a greater impact on liquid chromatography than Csaba Horváth.

Chromatographic purification of some 3-hydroxy-3-methylglutaryl coenzyme A reductase inhibitors

The purification of pravastatin, simvastatin and lovastatin in the sodium salt or lactone form and of mevastatin in the lactone form by reversed-phase displacement chromatography is presented. The mobile phases consisted of water or mixtures of water-methanol and water-acetonitrile. Six different displacers were successfully used. Up to 0.14 g of raw sample per gram of stationary phase was loaded on a column packed with silica-based octadecyl phase. Crude substances from 85 to 88% chromatographic purity were purified and at least 99.5% purity was achieved.

Displacement chromatography with on-column isomerization

Displacement chromatography was simulated for the separation of two feed components interconverting by a reversible first order reaction and with Langmuirian adsorption behavior. The study was prompted by recent interest in the isolation of cis and trans forms of peptides containing one or more peptidyl-proline residues when the isomerization reaction interferes with the separation. The parameter values used in the simulations are similar to those found experimentally by reversed-phase chromatography and capillary electrophoresis of phenylalanine-proline dipeptide. From the concentration profiles computed by the finite difference scheme, the dependence of both the yield and production rate on the temperature, column length, flow velocity and displacer concentration was evaluated. The most important operational variable of the system is the temperature as it affects both the kinetic and adsorption parameters. The yield and production rate of the component of interest were evaluated as a function of the column length and displacer concentration under conditions that facilitate its efficient separation and the plots show an optimum. Nonetheless, optimal conditions for yield and production rate were considerably different. In the temperature range from 2 to 42 degrees C, the yield always decreases with increasing temperatures and for all the cases, optimum yield by displacement mandates the use of conditions such as pH, solvent and temperature under which the rate of interconversion is reduced to a level where it does not palpably interfere with the separation. On the other hand, under certain conditions optimal production rate can be obtained at higher temperatures.

Chromatography in the downstream processing of biotechnological products

Chromatography techniques are essential for the isolation and purification of most of the high value products of modern biotechnology. The economically sensible and technically satisfactory downstream processing of a therapeutic protein, usually involves a number of chromatographic steps. Its development and optimization require considerable knowledge of the various physico-chemical and engineering aspects of biochemical chromatography. This review addresses the various modes of chromatography and the design of chromatographic separation processes from a biotechnologist's point of view. Strategies for optimizing the structure of the downstream process are outlined and scaling up consideration are discussed. The importance of the different chromatographic methods in research and development is estimated in an analysis of protein purification schemes recently published in the literature. Finally, examples of the application of chromatographic procedures for process scale product purification in the biotechnological industry are given.

Characterization of a tryptic digest by high-performance displacement chromatography and mass spectrometry

High-performance displacement chromatography (HPDC) provides a means of increasing the capacity of a chromatographic column, while maintaining the resolution afforded by high-performance liquid chromatographic (HPLC) instruments. The high capacity and high resolution of HPDC can be exploited in tryptic mapping to facilitate the characterization of a protein preparation. In this manner, minor constituents of the mixture, which may be difficult to isolate by conventional chromatographic methods, can be obtained in sufficient amounts to permit chemical characterization by established techniques. The isolation by HPDC of peptides obtained by digestion of recombinant human growth hormone (rhGH) and the subsequent characterization of the peptides are described. The identification of certain of these peptides revealed information on the specificity of trypsin for the substrate, rhGH, and for autolysis. Fractions from the HPDC tryptic map were collected and analyzed by electrospray ionization mass spectrometry (ESI-MS) either directly or following further separation by gradient elution HPLC. Fragment ions observed in the ESI mass spectra facilitated identification of peptides obtained by HPDC tryptic mapping.

High-performance displacement chromatography-mass spectrometry of tryptic peptides of recombinant human growth hormone

The combination of high-performance displacement chromatography with continuous flow fast atom bombardment (FAB)-mass spectrometry (MS) offers a means of overcoming the sample capacity limitations imposed by the low flow-rates tolerated in microbore systems employed for directly coupled liquid chromatography-MS. Displacement chromatography is performed at high concentrations with the same equipment and columns as typically used in chromatography at low concentrations. By using this mode of chromatography with a solution of cetyltrimethylammonium bromide as the displacer, the capacity of a reversed-phase column can be increased 50- to 100-fold for separation of a tryptic digest of biosynthetic human growth hormone. Despite the high load, the use of displacement chromatography allowed high-resolution separation of the complex mixture of eighteen major components. On-line analysis by continuous flow FAB-MS yielded high-quality spectra of these peptides and demonstrated that sharp, single-component bands can be obtained in this separation. Along with the major fragments, the chromatogram showed other peptides originating from protein variants in the sample, from non-specific cleavage in the enzymatic digest or from autolysis of trypsin. On-line analysis also allowed selective ion monitoring of the column effluent for individual peptides and confirmed the high efficiency and resolution obtained by preparative displacement separations on HPLC columns and equipment.

Displacement chromatography on cyclodextrin-silicas. III. Enantiomer separations

The feasibility of preparative enantiomer separations by displacement chromatography on analytical-scale beta-cyclodextrin-silica columns, operated in the reversed-phase mode, was demonstrated using the enantiomers of mephobarbital, hexobarbital, dansylleucine, dansylvaline and dansylphenylalanine as model solutes. The method development scheme (which relies on the determination of the elution-mode retention behavior and the adsorption isotherms of the solutes and the candidate displacers) described in Parts I and II can be used to select the appropriate displacers and the conditions leading to a successful displacement chromatographic separation. The importance of the displacer (both type and concentration) to the success of the displacement chromatographic separation is demonstrated.

Displacement chromatography on cyclodextrin-silicas. I. Separation of positional and geometrical isomers in the reversed-phase mode

The retention behaviour of several charged and uncharged solutes on beta-cyclodextrin-silica was studied as a function of the methanol concentration, ionic strength and pH of the eluent in order to develop efficient displacement chromatographic separations for positional and geometric isomers. These retention curves were used to predict the eluent (carrier solvent) compositions that result in solute retentions in excess of k' = 10. The adsorption isotherms of several cationic detergents were determined in these carrier solutions and were found to be convex. The adsorption isotherms of several positional isomers used as test solutes were also determined in these carrier solutions. The adsorption isotherms permitted the development of efficient displacement chromatographic separations for the isomers tested. Column loadings as high as 58 mg were achieved on a regular 4.6 mm I.D. analytical-scale cyclodextrin silica columns.

Mixed-bed ion-exchange columns for protein high-performance liquid chromatography

Protein retention is investigated on high-performance liquid chromatography columns packed with mixtures of ion exchangers. Retention factors are measured at both low and high salt concentrations in the eluent and their dependence on the bed composition is found to be linear in some cases, but non-linear in others. The physical basis for the observed non-linear retention behavior has not been established and an empirical mixing rule is employed to express the dependence of protein retention on bed composition. Protein separations are carried out on the mixed-bed columns by using gradient elution with increasing salt concentration and the process is modelled mathematically. The retention times predicted by computer calculations correspond closely to the experimental findings. Optimal selection of the mixed-bed composition and the gradient steepness for the separation of four proteins is illustrated by using the window diagram technique. Although the experimental results presented here deal with electrostatic interaction chromatography of proteins only the applicability of mixed sorbents is expected to extend to all branches of liquid chromatography. It is anticipated that mixed-sorbent columns will find extensive use in the large-scale purification of biological compounds and in routine analysis.

Preparative chromatography of proteins analysis of the multivalent ion-exchange formalism

Multivalent ion exchange is proposed as a generally applicable formalism to describe the non-linear chromatographic adsorption of biopolymers. Single- and multi-component isotherms are calculated that explicitly account for the influence of the mobile phase modulator concentration. Three regions of binding (strong, intermediate, and weak) are distinguished on the basis of strength of interaction, and the potential advantages of operating in the strong region for preparative purposes are pointed out. The inapplicability of the Langmuir isotherm in this region is demonstrated, and separation schemes that take advantage of the characteristic features of biopolymeric adsorption are described. The rectangular single-component ion-exchange isotherms are shown to reduce in the presence of competition to reversible concave-down forms.

High-performance displacement chromatography of melanotropins and their derivatives

Mixtures containing derivatives of the biological active peptide alpha-melanocyte stimulating hormone (alpha-MSH) or beta-melanocyte stimulating hormone (beta-MSH) were purified by using reversed-phase chromatography in the displacement mode. On a 250 x 4.6 mm octadecyl silica column and with instrumentation used in analytical high-performance liquid chromatography about 30 mg of the peptide mixture were separated by using an aqueous solution of benzyldimethyldodecylamonium bromide as the displacer in a single chromatographic run. The results demonstrate the advantages of displacement over elution in preparative chromatography of peptides on the scale of tens of milligrams that is typical for physiological tissue extracts and in solid-phase peptide synthesis.

Displacement chromatography of biomolecules

Displacement chromatography was used for the preparative-scale separation of peptides, antibiotics, and proteins. The feed components were both purified and concentrated during the separation processes. The components of a peptide mixture were separated on a reverse-phase analytical column using 2-(2-butoxyethoxy) ethanol as the displacer. The use of organic modifiers in the carrier along with an elevated column temperature of 45 degrees C enabled the efficient separation of relatively hydrophobic peptides by displacement chromatography. In addition, the throughput of the process was significantly increased by carrying out the separation at an elevated flow-rate with no adverse effect on product purity. The antibiotic cephalosporin C was isolated from impurities in a fermentation broth using 2-(2-butoxyethoxy)ethanol as the displacer along with a step change in column temperature. The proteins cytochrome c and lysozyme were purified on a weak cation-exchanger column using cationic polymers as the displacers. While polymers of 60 and 20 kilodaltons were both found to be good displacers for these proteins, only the lower molecular weight polymer was readily removed from the column by standard regeneration techniques.