Comparison of anion-exchange and hydroxyapatite displacement chromatography for the isolation of whey proteins

Application of Ion Exchange and Adsorption Techniques for Separation of Whey Proteins from Bovine Milk

Background:

The world production of whey was estimated to be more than 200 million tons per year. Although whey is an important source of proteins with high nutritional value and biotechnological importance, it is still considered as a by-product of the dairy industry with low economic value due to low industrial exploitation. There are several challenges in the separation of whey proteins: low concentration, the complexity of the material and similar properties (pI, molecular mass) of some proteins.

Methods:

A narrative review of all the relevant papers on the present methodologies based on ion-exchange and adsorption principles for isolation of whey proteins, known to the authors, was conducted.

Results:

Traditional ion-exchange techniques are widely used for the separation and purification of the bovine whey proteins. These methodologies, based on the anion or cation chromatographic procedures, as well as combination of aforementioned techniques are still preferential methods for the isolation of the whey proteins on the laboratory scale. However, more recent research on ion exchange membranes for this purpose has been introduced, with promising potential to be applied on the pilot industrial scale. Newly developed methodologies based either on the ion-exchange separation (for example: simulated moving bed chromatography, expanded bed adsorption, magnetic ion exchangers, etc.) or adsorption (for example: adsorption on hydroxyapatite or activated carbon, or molecular imprinting) are promising approaches for scaling up of the whey proteins’ purification processes.

Conclusion:

Many procedures based on ion exchange are successfully implemented for separation and purification of whey proteins, providing protein preparations of moderate-to-high yield and satisfactory purity. However, the authors anticipate further development of adsorption-based methodologies for separation of whey proteins by targeting the differences in proteins’ structures rather than targeting the differences in molecular masses and pI. The complex composite multilayered matrices, including also inorganic components, are promising materials for simultaneous exploiting of the differences in the masses, pI and structures of whey proteins for the separation.

Separation of plasmid DNA from protein and bacterial lipopolysaccharides using displacement chromatography

The preparation of plasmid DNA at large scale constitutes a pressing problem in bioseparation. This paper describes a first investigation of displacement chromatography as a means to separate plasmid DNA (4.7 kb) from E. coli lipopolysaccharides and protein (holo transferrin), respectively. Displacement chromatography has advantages in this regard, since the substance mixture is resolved into rectangular zones of the individual components rather than into peaks. Thus a higher total concentration can be maintained in the pooled product fractions. Hydroxyapatite (type I and II) and anion exchange stationary phases were included in the experiments. In addition to a conventional anion exchange column packed with porous particles, the recently introduced continuous bed UNOTM anion exchange column was investigated. No DNA purification was possible with either hydroxyapatite material. Conventional particle based columns in general were not suited to the separation of any two substances varying considerably in molecular mass, e.g. plasmid DNA and standard protein. Presumably, the direct competition for the binding sites, which is essential in displacement chromatography, was restricted by the size dependency of the accessible stationary phase surface area in this case. Better results were obtained with the continuous bed column, in which the adsorptive surface coincides with the walls of the flow through pores. As a result the accessible surface does not vary as much with the size of the interacting molecules as for the conventional stationary phase materials. Sharper transitions were also observed between substance zones recovered from the UNOTM column. The steric mass action model was used to aid method development in case of the anion exchange approach. While further research in obviously necessary, displacement chromatography on continuous bed columns has been shown to be capable of separating plasmid DNA from typical impurities.

Detection of trace proteins in multicomponent mixtures using displacement chromatography

Model protein feed mixtures containing three abundant and seven trace proteins at various concentrations were identified and employed in a series of displacement experiments. Reversed-phase liquid chromatography (RPLC) and matrix assisted laser desorption ionization-time-of-flight (MALDI-TOF) mass spectrometry were used to evaluate the compositions of both the feed mixtures and effluent fractions from the displacement experiments. The results demonstrated that trace proteins were focused at the boundaries between the abundant solutes where they were enriched and concentrated. For many of the multicomponent feed mixtures, mass spectrometry analyses of the displacement column effluent fractions resulted in the identification of trace proteins that were not detectable in the feed. In addition, the use of minimal or no salt in the carrier solutions enabled the analysis of displacement fractions by direct infusion mass spectrometry. These results are significant in that they indicate that while the presence of abundant proteins can often be problematic for the detection of trace components, displacement chromatography may be able to employ these abundant proteins to focus trace proteins in the displacement train, thus facilitating detection.

Purification of the two major proteins from whey concentrate using a cation-exchange selective adsorption process

The packed-bed adsorption and elution of aqueous solutions of whey concentrate powders were investigated at pH 3.7 using a 5-mL SP Sepharose FF column to separate and isolate two major proteins namely, alpha-lactalbumin (ALA) and beta-lactoglobulin (BLG) from these solutions. ALA displaced and eluted BLG from the column in a pure form. Pure ALA could then be eluted with good recovery. A novel consecutive two-stage separation process was developed to separate ALA and BLG from whey concentrate mixtures. Almost all of the BLG in the feed was recovered, with 78% being recovered at 95% purity and a further 20% at 86% purity. In addition, 67% of ALA was recovered, 48% at 54% purity and 19% at 60% purity.

Synthesis and characterization of fluorescent displacers for online monitoring of displacement chromatography

One of the major impediments to the implementation of displacement chromatography for the purification of biomolecules is the need to collect fractions from the column effluent for time-consuming offline analysis. The ability to employ direct online monitoring of displacement chromatography would have significant implications for applications ranging from analytical to preparative bioseparations. To this end, a set of novel fluorescent displacers were rationally designed using known chemically selective displacers as a template. Fluorescent cores were functionalized with different charge moieties, creating a homologous library of displacers. These compounds were then tested on two protein pairs, alpha-chymotrypsinogen A/ribonuclease A and cytochrome c/lysozyme, using batch and column displacement experiments. Of the synthesized displacers, two were found to be highly selective while one was determined to be a high-affinity displacer. Column displacements using one of the selective displacers yielded complete separation of both protein pairs while facilitating direct online detection using UV and fluorescence detection. Saturation transfer difference NMR was also carried out to investigate the binding of the fluorescent displacers to proteins. The results indicated a selective binding between the selective displacers and alpha-chymotrypsinogen A, while no binding was observed for ribonuclease A, confirming that protein-displacer binding is responsible for the selectivity in these systems. This work demonstrates the utility of fluorescent displacers to enable online monitoring of displacer breakthroughs while also acting as efficient displacers for protein purification.

Displacement chromatography of proteins on hydrophobic charge induction adsorbent column

Displacement chromatography of protein mixtures is proposed on hydrophobic charge induction chromatography (HCIC). We have used an HCIC medium, MEP-Hypercel as the stationary phase and a quaternary ammonium salt, benzethonium chloride, as the displacer. It was found that the multiple interactions between proteins/displacer and the HCIC sorbent, i.e. hydrophobic interaction and charge repulsion, enabled a greater flexibility for the design of displacement processes and ease of column regeneration by adjustment of pH. The capacity factors of proteins and displacers were used to predict their performances in column displacement, and the experimental results agreed well with the prediction. An isotachic displacement train of lysozyme and alpha-chymotrypsinogen A was formed with benzethonium chloride as the displacer at pH 5.0 with good yields and purities of the two proteins. Column regeneration was efficiently achieved by charge repulsion between the displacer and the adsorbent at lower pH values (pH 3 and 4). The results indicate that the displacement chromatography on HCIC is a good alternative to traditional hydrophobic displacement chromatography.

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.

Improved purification of β-lactoglobulin from acid whey by means of ceramic hydroxyapatite chromatography with sodium fluoride as a displacer

The successful separation of beta-lactoglobulin from other bovine whey proteins was performed by ceramic hydroxyapatite chromatography with a fluoride ion gradient in phosphate buffer as displacement agent. The method was applied to acid whey originating from milk of healthy as well as of mastitic cows. beta-Lactoglobulin was completely eluted in one peak at a fluoride concentration of about 0.6 mol/l. The purity of beta-lactoglobulin in this fraction was at least 96% if whey from healthy milk was processed. Co-eluted contaminants are traces of immunoglobulin G, serum albumin and lactoferrin. In case of mastitic whey the proportion of beta-lactoglobulin is diminished as the amounts of immunglobulin G, serum albumin and lactoferrin are increased within this fraction. Size exclusion chromatography on Superdex 75 pg effectively removed contaminants resulting in a purity for beta-lactoglobulin from normal whey of approximately 99%. The yield of beta-lactoglobulin from physiological whey was 50-55% referring to the fraction highly enriched with beta-lactoglobulin by hydroxyapatite chromatography. In case of mastitic milk the higher amounts of contaminants were also removed successfully by size exclusion chromatography.

Manufacture and use of dairy protein fractions

Fractionation of the mixture of proteins found in milk and whey to form pure, individual dairy protein fractions might allow individuals with special nutritional needs to tailor their diet to improve health. Ion exchange process chromatography was examined for this purpose using selective elution to release separately the proteins bound from whey and produce several protein fractions. Alternatively, bound proteins were released all at once to make a whey protein isolate. Prototype beverages containing these proteins were examined for clarity before and after thermal processing. Beverages containing whey protein isolate were clear at pH 2-7 before heating, but only beverages at pH <or= 3.0 were clear after thermal processing (88 degrees C, 120 s). Beverages at higher pH were made clear after heating by addition of food-grade lauryl sulfate, which prevented aggregation of the denatured proteins formed during thermal processing. Alternatively, thermally processed clear beverages at pH 3-7 were possible using the whey protein glycomacropeptide. Because of the balance between sweetness and acidity, beverages with a pH greater than carbonated soft drinks and juices (pH 2.5-3) might remain palatable using less sugar. Development of high-protein low-carbohydrate beverages might provide health benefits for individuals suffering from diabetes, obesity, and hypercholesterolemia, especially when these beverages contain dairy protein fractions known to be high in essential amino acids and branched-chain amino acids.

Investigation of particle-based and monolithic columns for cation exchange protein displacement chromatography using poly(diallyl-dimethylammonium chloride) as displacer

The overall topic of the investigation was the separation of basic proteins by cation exchange displacement chromatography. For this purpose two principal column morphologies were compared for the separation of ribonuclease A and alpha-chymotrypsinogen, two proteins found in the bovine pancreas. These were a column packed with porous particles (Macro-Prep S, 10 microm, 1000 A) and a monolithic column (UNO S1). Both columns are strong cation exchangers, carrying -SO3(-)-groups linked to a hydrophilic polymer support. Poly(diallyl-dimethylammonium chloride) (PDADMAC), a linear cationic polyelectrolyte composed of 100-200 quaternary pyrrolidinium rings, was used as displacer. The steric mass action (SMA) model and, in particular, the operating regime and dynamic affinity plots were used to aid method development. To date the SMA model has been applied primarily to simulate non-linear displacement chromatography of proteins using low molar mass displacers. Here, the model is applied to polyelectrolytes with a molar mass below 20000 g mol(-1), which corresponds to a degree of polymerization below 125 and an average contour length of less than 60 nm. The columns were characterized in terms of the adsorption isotherms (affinity, capacity) of the investigated proteins and the displacer.

Whey proteins as a model system for chromatographic separation of proteins

Although chromatographic separation of whey proteins has been considered too expensive, whey may serve as an excellent model mixture to investigate and validate the use of simulation tools in the development and optimization of chromatographic separations and the outcome could easily be utilized since the model system has an intrinsic value. Besides, milk from transgenic animals could be an attractive source of pharmaceuticals which must be separated from the other proteins in the milk. Several whey proteins are of interest especially, alpha-lactalbumin, beta-lactoglobulins, immunoglobulins, lactoperoxidase, and lactoferrin. The scope of the project is to develop a consistent set of chromatographic data for whey proteins including isotherms, transport properties and scale-up studies and to develop the appropriate models for the anion exchangers Q-Sepharose XL, Source 30Q, Ceramic Q-HyperD F, and Merck Fractogel EMD TMAE 650 (S). In this work we have determined and correlated gradient and isocratic retention volumes in the linear range of the isotherm for alpha-lactalbumin, beta-lactoglobulin A and B, and bovine serum albumin at a pH from 6 to 9 at various NaCl concentrations.

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.

One-step separation from lactose: recovery and purification of major cheese-whey proteins by hydroxyapatite--a flexible procedure suitable for small- and medium-scale preparations

The recovery of cheese-whey proteins and lactose represents an important task both in environmental and in food sciences. Optimization of whey processing requires the quantitative separation of whey proteins from lactose, lower costs, harmless environmental impact, flexibility in protein recovery, and adaptability of the process to type and amount of available whey. Here we present a method based on the use of self-made, low-price, and nontoxic hydroxyapatite for one-step separation of lactose (non adsorbed) from bovine whey proteins (adsorbed). Recovery of proteins can be performed with high flexibility. Total protein fraction can be eluted with 0.4 M phosphate at pH 7.0. In alternative, proteins can be recovered in pairs with 0.4 M phosphate but at different pH's. About 56% of the proteins, primarily alpha-lactalbulmin and IgG, were eluted at pH 5.0. The other major proteins, beta-lactoglobulin and BSA, were eluted at pH 6.0. Fractions eluted with the two first eluants at pH 5.0 and pH 6.0 were applied to a Superdex 75 column for final purification by gel filtration. This method provides flexibility in whey protein recovery and quantitative separation of proteins from lactose before ultrafiltration and nanofiltration.

Hydrophobic displacement chromatography of proteins

Displacement chromatography of proteins was successfully carried out in both hydrophobic interaction and reversed-phase chromatographic systems using low-molecular weight displacers. The displacers employed for hydrophobic displacement chromatography were water soluble, charged molecules containing several short alkyl and/or aryl groups. Spectroscopy was employed to verify the absence of structural changes to the proteins displaced on these hydrophobic supports. Displacement chromatography on a reversed-phase material was employed to purify a growth factor protein from its closely related variants, demonstrating the high resolutions that can be achieved by hydrophobic displacement chromatography. This process combines the high-resolution/high-throughput characteristics of displacement chromatography with the unique selectivity of these hydrophobic supports and offers the chromatographic engineer a powerful tool for the preparative purification of proteins.

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.

Development of a downstream process for the isolation and separation of monoclonal immunoglobulin A monomers, dimers and polymers from cell culture supernatant

The isolation and separation of the molecular variants of monoclonal IgA from cell culture supernatants is possible using several filtration and ion-exchange chromatography steps, followed by size-exclusion chromatography for the actual separation of the molecular variants. The latter step is especially time consuming and laborious. This report presents possible improvements of the procedure. Use of the displacement rather than the elution mode may render the ion-exchange step more productive (higher product concentrations and space-time yield). For the final separation of the molecular variants, hydroxyapatite (HA) elution chromatography can serve as an alternative to size-exclusion chromatography. By using an optimized, complex phosphate gradient, the IgA dimers can be separated quantitatively from the monomers and higher oligomers. It may in individual cases be necessary to use a size-exclusion polishing step to reach the required final degree of purity, however, the amount of material to be processed is reduced to such an extend by the HA-step, that the overall process is still more productive. Buffer pH and flow-rate as well as the stationary phase material used were additional factors considered during the optimization of the HA elution chromatography. HA-displacement chromatography resulted only in a concentration of the overall IgA fraction, but not in a separation of the molecular forms.