Tandem separation schemes for preparative high-performance liquid chromatography of proteins

The effect of multi-component adsorption on selectivity in ion exchange displacement systems

This paper examines chemically selective displacement chromatography using affinity ranking plots, batch displacer screening experiments, column displacements, multi-component adsorption isotherms and spectroscopy. The affinity ranking plot indicated that the displacers, sucrose octasulfate (SOS) and tatrazine, should possess sufficient affinity to displace the proteins amyloglucosidase and apoferritin over a wide range of operating conditions. In addition, the plots indicated that the separation of these proteins by displacement chromatography would be extremely difficult. Further, the two proteins were shown to have very similar retention times under shallow linear gradient conditions. When batch displacement experiments were carried out, both tartrazine and SOS exhibited significant selectivity differences with respect to their ability to displace these two proteins, in contrast to the affinity ranking plot results. Column displacement experiments carried out with sucrose octasulfate agreed with the predictions of the affinity ranking plots, with both proteins being displaced but poorly resolved under several column displacement conditions. On the other hand, column displacement with tartrazine as the displacer resulted in the selective displacement and partial purification of apoferritin. Single- and multi-component isotherms of the proteins with or without the presence of displacers were determined and were used to help explain the selectivity reversals observed in the column and batch displacement experiments. In addition, fluorescence and CD spectra suggested that the displacers did not induce any structural changes to either of the proteins. The results in this paper indicate that multi-component adsorption behavior can be exploited for creating chemically selective displacement separations.

Stationary phase effects on the dynamic affinity of low-molecular-mass displacers

In this paper, the selectivity of a variety of cation-exchange stationary phases was investigated using a homologous series of displacer molecules based on pentaerythritol. These displacers were derived from pentaerythritol and contained either four trimethyl ammonium groups [pentaerythrityl-(trimethylammonium chloride)4, PE(TMA)4], benzene rings [pentaerythrityl-(benzyl dimethylammonium chloride)4, PE(DMABzCl)4], heptyl groups [pentaerythrityl-(heptyl dimethylammonium iodide)4, PE(DMAHepI)4] or cyclohexyl groups [pentaerythrityl-(cyclohexyl dimethylammonium iodide)4, PE(DMACyI)4]. This series enabled us to probe the secondary interactions that can play a role in the affinity of low-molecular-mass displacers for different stationary phases. The relative affinities of these displacers were examined using a displacer ranking plot based on the steric mass action (SMA) isotherm model. While hydrophobicity and aromaticity played important roles in generating the affinity to the hydrophilized polystyrene-divinylbenzene (Source 15S) and polymethacrylate-based (Toyopearl 650M) resins, these secondary interactions had a minimal impact on the selectivity in agarose resins coated with dextran (SP Sepharose XL), "gel in a shell" (S Ceramic HyperD F), and monolithic (Bio-Rad Uno S6) cation-exchange materials. Further, the results with a tentacular stationary phase (Fractogel EMD) suggest that the alkyl chains on PE(DMAHepI)4 play an important role in increasing the affinity, possibly because of strong interactions between the alkyl moiety and the polymer matrix as well as between the charged groups and the polyelectrolyte tentacles. The results of this study provide insight into the design of high affinity, low-molecular-mass displacers for different cation-exchange stationary phase materials.

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.

Protein displacement in dye-ligand chromatography using neutral and charged polymers

Displacement chromatography was demonstrated to perform separations efficiently under mass-overloaded conditions, offering advantages such as increased product recovery and purity, superior resolving power, and concentration and purification in a single processing step. The use of water-soluble polymers for protein displacement in dye-ligand chromatography was initiated in our laboratory. The polymers for displacement were selected using differences spectroscopy to monitor their interactions with a dye-ligand in solution. Non-charged polymers such as poly(N-vinyl pyrrolidone) and poly(N-vinyl caprolactam) efficiently displaced lactate dehydrogenase from porcine muscle from a Blue Sepahrose column. The latter polymer, being thermosensitive, could be easily removed from the eluate and recovered by precipitation at 45 degrees C and low-speed centrifugation. The positively charged polymer poly(ethylene imine) proved to be an even more efficient displacer. The dye-ligand column could be regenerated after application of displacer either by washing with a solution of the soluble ligand Cibacron Blue (in the case of non-charged polymers) or by washing with highly alkaline solutions containing polyanions (in the case of poly(ethylene imine)) The latter formed a soluble complex with poly(ethylene imine) and stripped the column from the polymer.

Cation-exchange displacement chromatography for the purification of recombinant protein therapeutics from variants

Removal of low level impurities that are closely related to the bioproduct is a commonly encountered challenge in the purification of biopharmaceuticals. These separations are typically carried out by using shallow linear salt gradients at relatively low column loadings, significantly limiting the throughput of the purification process. In this manuscript we examine the utility of displacement chromatography for the purification of recombinant human brain-derived neurotrophic factor, rHuBDNF. The utility of displacement chromatography is compared to gradient elution for the removal of variants of the rHuBDNF. The results demonstrate that displacement chromatography is capable of achieving high yields and purity at high column loadings. Displacements developed on 20 microns and 50 microns cation-exchange resins are shown to provide 8-fold and 4.5-fold increases in production rates, respectively, when compared to an existing linear gradient elution operation. These results demonstrate the efficacy of displacement chromatography for the purification of therapeutic proteins from complex feed streams.

Alginate as a displacer for protein displacement chromatography

Alginate use in displacement chromatography as a displacer has been studied. The experiments showed that untreated alginate is the basis of potential displacer for displacement chromatography, but needs to be cleaved into smaller chains. Alginate treated with ultrasound, which cleaves alginate into shorter polysaccharide chains, gave better displacement than untreated alginate, while alginate subjected to limited acid hydrolysis gave the best results in displacement chromatography. It was found that the mixture of ovalbumin and beta-lactoglobulin separated well, and several components of ovalbumin were also separated and purified when alginate hydrolysate was used as a displacer. beta-Lactoglobulins A and B, which have the same molecular weight and differ in isoelectric point by only 0.1 pH units, were displaced from Q-Sepharose by alginate hydrolysate.

Gram-scale purification of phosphorothioate oligonucleotides using ion-exchange displacement chromatography

The purification of oligonucleotides by ion-exchange displacement chromatography is demonstrated on the gram-scale. Using a 50 mmD x 100 mmL (203 ml) column operated in the displacement mode, 1.2 g of a 24mer phosphorothioate oligonucleotide was purified. Product yield for this separation was 70% (780 mg) at a purity of 96.4% and the mass balance recovery of all oligonucleotide was 97.5%. The displacement purification of four additional phosphorothioate oligonucleotides ranging in length from 18 to 25 bases is also demonstrated on the semi-preparative (10-50 mg) scale. All of these oligonucleotides were purified using similar displacement conditions and typical results were 60% yield at 96% purity. The displacement portion of these separations required <15 min and total cycle time including equilibration, feed loading and regeneration can be performed in under 30 min. These results seem to indicate that displacement chromatography may be amenable to generalizations in separation protocol that would greatly reduce the effort required to obtain an optimized purification scheme for moderately long oligonucleotides.

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.

Preparative chromatography in biotechnology

The field of preparative chromatography has experienced several important advances recently in both the structure of chromatographic materials and modes of chromatographic operation. This review presents recent applications of preparative chromatography in biotechnology, as well as novel stationary phase materials and engineering approaches to preparative chromatographic bioseparations.

Rapid displacement chromatography of melittin on micropellicular octadecyl-silica

Rapid high-performance liquid chromatographic analysis and displacement purification of melittin and its variants were carried out by reversed-phase chromatography. High speed of separation was achieved by the use of columns packed with a micropellicular stationary phase consisting of a thin C18 hydrocarbonaceous layer on the surface of 2-microns fluid-impervious silica microspheres at elevated temperature. In the case of melittin from bee venom or its synthetic variants the plots of the logarithmic retention factor against acetonitrile concentration in the eluent were straight lines whereas the van't Hoff plots in the temperature range from 20 to 80 degrees C were non-linear. Purification of melittins by displacement was carried out with benzyldimethylhexadecyl ammonium chloride as the displacer. In a 20-min displacement run at 40 degrees C about 5 mg of highly pure melittin were isolated from 10 mg of synthetic mixture by using a 105 x 4.6 mm column. The results demonstrate that columns packed with micropellicular sorbents not only facilitate rapid high-performance liquid chromatographic analysis but are also suitable for fast peptide purification with high recovery.

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.