High-performance hydrophobic interaction chromatography of proteins

A new, weakly hydrophobic, high-performance liquid chromatography column has been developed for the separation of native proteins based on their relative hydrophobicities. Starting with a covalently bound, hydrophilic polyamine matrix, packing materials were synthesized through acylation with anhydrides and acid chlorides of increasing chain length to obtain increasingly hydrophobic surfaces. Proteins in aqueous buffers were induced to bind hydrophobically to the columns by the use of high salt concentrations in the mobile phase. Elution was achieved by decreasing the ionic strength of the solvent in a linear gradient. A mixture of cytochrome c, conalbumin, and beta-glucosidase was used as a standard to test the resolving power of newly synthesized columns. On a 4-cm butyrate column, baseline resolution was achieved in 20 min with a gradient of 3.0 mu sodium sulfate in 0.1 M potassium phosphate buffer, pH 7.0, to water. The static loading capacity for each column was determined using a hemoglobin binding assay. Capacities normally ranged between 150 and 180 mg of hemoglobin per gram of support. Since proteins are not denatured in hydrophobic interaction chromatography, enzymes eluted from the column retained enzymatic activity. Samples of alpha-amylase and beta-glucosidase ranging in size from 10 to 200 micrograms were recovered from the butyrate column with greater than 92% enzymatic activity in all cases. In a single trial, the enzyme citrate synthase was recovered from the benzoate column with 92% retention of enzymatic activity.     

Separation of the proteins present in pancreatic juice using hydrophobic interaction chromatography

We have previously described a method for separating pancreatic juice proteins by reversed-phase HPLC. However, the solvents used in such a system denature the proteins, whose characterization therefore depends solely on molecular weight determinations. We have therefore tested the suitability of hydrophobic interaction chromatography as an alternative method of separation. Using a TSK phenyl 5PW column with a decreasing, four-stage ammonium sulfate concentration gradient, it was possible to separate the major proteins in rat pancreatic juice. The identity of each protein was confirmed by measuring its molecular weight and by assaying its enzyme activity. Hydrophobic interaction chromatography represents an improved system for separating pancreatic secretory enzymes in active form.     

Separation of human vitamin K-dependent coagulation proteins using hydrophobic interaction chromatography

A rapid and simple method was developed to separate human vitamin K-dependent plasma proteins from each other, yielding virtually homogeneous pools. The purification technique is based on the single use of hydrophobic interaction chromatography, starting from prothrombin concentrate (PC or DEFIX, also termed factor IX concentrate) as initial material. Phenyl-sepharose HP demonstrated optimal separation by comparing several hydrophobic resins as well as resins used in standard procedures like immobilised heparin and Cibacron blue. Under ideal conditions, factor X could be separated in a single step as well as prothrombin. Factor IX co-eluted with other minor proteins. Focus was given only on these three proteins due to their relative abundance. Complete separation of all proteins present in the starting material was achieved by MonoQ anion-exchange chromatography following the phenyl-sepharose run. The resulting purified material could be demonstrated to be of equal or higher purity than using described methods. This strategy employing hydrophobic interaction chromatography for blood macromolecules could be of immense value for purifying the human vitamin K-dependent proteins and represents a considerable simplification over other purification schemes. It not only involves minimal sample handling but also can be readily up-scaled and is a cost-efficient alternative.     

Calorimetry for studying the adsorption of proteins in hydrophobic interaction chromatography

Hydrophobic interaction chromatography is a very popular chromatography method for purification of proteins and plasmids in all scales from analytical to industrial manufacturing. Despite this frequent use, the complex interaction mechanism and the thermodynamic aspects of adsorption in hydrophobic interaction chromatography are still not well understood. Calorimetric methods such as isothermal titration calorimetry and flow calorimetry can help to gain a deeper understanding of the adsorption strength, the influence of salt type and temperature. They can be used to study conformational changes of proteins, which are often associated with the adsorption in hydrophobic interaction chromatography. This review offers a detailed introduction into the thermodynamic fundamentals of adsorption in hydrophobic interaction chromatography with a special focus on the potential applications of isothermal titration calorimetry and flow calorimetry for studying specific problems and relationships of the adsorption behavior of proteins and its various influencing factors. Models for characterizing conformational changes upon adsorption are presented together with methods for assessing this problem for different proteins and stationary phases. All of this knowledge can contribute greatly to forming a sound basis for method development, process optimization and finding modelling strategies in hydrophobic interaction chromatography.     

Fractionation and recovery of whey proteins by hydrophobic interaction chromatography

A method for the recovery and fractionation of whey proteins from a whey protein concentrate (80%, w/w) by hydrophobic interaction chromatography is proposed. Standard proteins and WPC 80 dissolved in phosphate buffer with ammonium sulfate 1 M were loaded in a HiPrep Octyl Sepharose FF column coupled to a fast protein liquid chromatography (FPLC) system and eluted by decreasing the ionic strength of the buffer using a salt gradient. The results showed that the most hydrophobic protein from whey is α-lactalbumin and the less hydrophobic is lactoferrin. It was possible to recover 45.2% of β-lactoglobulin using the HiPrep Octyl Sepharose FF column from the whey protein concentrate mixture with 99.6% purity on total protein basis.     

One-step purification of bacterial lipid macroamphiphiles by hydrophobic interaction chromatography

Bacterial lipid macroamphiphiles extracted with phenol/water can be purified in one step by hydrophobic interaction chromatography. Lipids and the major part of protein are separated from macroamphiphiles during phenol/water extraction. Coextracted nucleic acids, polysaccharides, and residual protein are effectively removed by column chromatography on octyl-Sepharose whereby macroamphiphiles are primarily adsorbed and later eluted with a buffered propanol gradient. The procedure is applicable to macroamphiphiles with various lipid structures as was demonstrated using the diacylglycerol-containing lipoglycan of Micrococcus luteus, the lipid A-containing lipopolysaccharide of Salmonella typhimurium, and the diglyceryl tetraether lipoglycans of Thermoplasma acidophilum and Thermoplasma volcanicum. On elution from octyl-Sepharose, separation into molecular species of different compositions was observed with the lipopolysaccharide of S. typhimurium and the lipoglycan of T. volcanicum. It was also shown that, after phenol/water extraction, membrane lipids are completely recoverable from the phenol layer, which makes it possible to isolate lipids along with macroamphiphiles from the same sample of bacteria.     

Separation of nucleic acids and chromatin proteins by hydrophobic interaction chromatography

A procedure by which chromatin proteins (histones and non-histones) can be rapidly separated from nucleic acids by hydrophobic interaction chromatography is described. The procedure is carried out under non-rigorous conditions that must be assumed to induce little irreversible change in the biological properties of most proteins. More than 90% (w/w) of the chromatin proteins can be retained by hydrophobic interaction while nucleic acids pass quantitatively through the columns. By gradient elution of the columns the histones can be divided into fractions containing H1, H2A/H2B and H3/H4, and at the same time a subfractionation of the non-histone proteins is obtained. Protein recovery depends on the type of column used, but exceeds 80% (w/w) with even the most strongly binding hydrophobic matrix investigated.     

Enrichment of serum amyloid proteins by hydrophobic interaction chromatography combined with two-dimensional electrophoresis with immobilised pH gradients

Serum amyloid A protein was subjected to one-step octyl-Sepharose extraction in three different dimensions. Elution was performed partly without UV recording, and with urea or guanidine-based buffers. The eluent was applied directly to denaturing two-dimensional electrophoresis with immobilised pH gradient, or octyl-Sepharose extracted fractions were pooled and lyophilised before application. Proteins were characterised by N-terminal analysis or mass spectrometry. In most of the species that were studied, previously undescribed serum amyloid proteins were detected. Compared to conventional strategies, the presented techniques are more rational and yield more comprehensive information. The presented data also provide a basis for novel perspectives regarding certain inflammatory conditions.     

Crossed hydrophobic interaction immunoelectrophoresis: An analytical method for detection of amphiphilic proteins in crude mixtures and for prediction of the result of hydrophobic interaction chromatography

Crossed hydrophobic interaction immunoelectrophoresis is an analytical technique in which the principles of quantitative immunoelectrophoresis and hydrophobic interaction are directly combined. Using phenyl-Sepharose as hydrophobic (amphiphilic) matrix we have shown how the method permits detection of amphiphilic proteins in three model systems: native- and trypsinated intestinal brush border aminopeptidase, serum proteins, and detergent-solubilized erythrocyte proteins. In the case of first system the relative amounts of the two forms of the enzyme have been determined using immunochemical quantification. Comparison of the present method with column hydrophobic interaction chromatography reveals concordant results for both serum and erythrocyte proteins. Tests of some alkyl-substituted agaroses show that they work in a manner similar to phenyl-Sepharose.     

Characterization of denatured proteins by hydrophobic interaction chromatography: a preliminary study

In this preliminary study hydrophobic interaction chromatography (HIC) is proposed as a good tool in order to detect conformational changes induced by chemical denaturants in two globular proteins, cytochrome C (Cyt C) and myoglobin (MYO). Alterations in protein structure were manifested chromatographically by reproducible changes in peak heights, retention time, and appearance of multiple peaks. The HIC behavior of the two model proteins denatured by guanidinium thyocyanate (GdmSCN) was investigated, keeping constant various concentrations of urea in the mobile phase in a TSK-Gel Phenyl-5PW column (TosoBiosep). Suitable elution conditions provide evidence of the simultaneous presence of two denatured forms in the case of MYO, and sequential different denatured states of Cyt C.     

Probing the interaction forces between hydrophobic peptides and supported lipid bilayers using AFM

Despite the vast body of literature that has accumulated on tilted peptides in the past decade, direct information on the forces that drive their interaction with lipid membranes is lacking. Here, we attempted to use atomic force microscopy (AFM) to explore the interaction forces between the Simian immunodeficiency virus peptide and phase-separated supported bilayers composed of various lipids, i.e. dipalmitoylphosphatidylcholine, dioleoylphosphatidylcholine, dioleoylphosphatidic acid and dipalmitoylphosphatidylethanolamine. Histidine-tagged peptides were attached onto AFM tips terminated with nitrilotriacetate and tri(ethylene glycol) groups, an approach expected to ensure optimal exposure of the C-terminal hydrophobic domain. Force-distance curves recorded between peptide-tips and the different bilayer domains always showed a long-range repulsion upon approach and a lack of adhesion upon retraction, in marked contrast with the hydrophobic nature of the peptide. To explain this unexpected behaviour, we suggest a mechanism in which lipids are pulled out from the bilayer due to strong interactions with the peptide-tip, in agreement with the very low force needed to extract lipids from supported bilayers.     

Bifunctional adsorbents for hydrophobic displacement chromatography of proteins

The separation of pancreatic trypsinogen and alpha-chymochypsinogen A by displacement chromatography was tested on a bifunctional adsorbent containing both butyl and carboxymethyl groups. Methacrylic triblock copolymer was synthesized and used as the displacer. Compared to the displacement results on commercial Butyl-Sepharose, it was found that both the separation and recovery of trypsinogen and alpha-chymochypsinogen A were improved. Adsorption isotherms of proteins were measured on both the commercial Butyl-Sepharose and the synthesized bifunctional adsorbents. It was found that the improvement of protein separation on bifunctional adsorbents was attributed to the alteration of the adsorption of trypsinogen. Charge repulsion between trypsinogen and the negatively charged carboxymethyl groups may account for the alteration. In addition, taking advantage of the effect of charge repulsion, the column regeneration became much easier on the column packed with bifunctional adsorbents.     

Depletion of highly abundant proteins in blood plasma by hydrophobic interaction chromatography for proteomic analysis

The proteomic analysis of plasma is extremely complex due to the presence of few highly abundant proteins. These proteins have to be depleted in order to detect low abundance proteins, which are likely to be of biomedical interest. In this work it was investigated the applicability of hydrophobic interaction chromatography (HIC) as a plasma fractionation method prior to two-dimensional gel electrophoresis (2DGE). The average hydrophobicity of the 56 main plasma proteins was calculated. Plasma proteins were classified as low, medium and highly hydrophobic through a cluster analysis. The highly abundant proteins showed a medium hydrophobicity, and therefore a HIC step was designed to deplete them from plasma. HIC performance was assessed by 2DGE, and it was compared to that obtained by a commercial immuno-affinity (IA) column for albumin depletion. Both methods showed similar reproducibility. HIC allowed partially depleting α-1-antitrypsin and albumin, and permitted to detect twice the number of spots than IA. Since albumin depletion by HIC was incomplete, it should be further optimized for its use as a complementary or alternative method to IA.     

The effects of arginine on protein binding and elution in hydrophobic interaction and ion-exchange chromatography

Arginine is effective in suppressing aggregation of proteins and may be beneficial to be included during purification processes. We have shown that arginine reduces non-specific protein binding in gel permeation chromatography and facilitates elution of antibodies from Protein-A columns. Here we have examined the effects of arginine on binding and elution of the proteins during hydrophobic interaction (HIC) and ion- exchange chromatographies (IEC) using recombinant monoclonal antibodies (mAbs) and human interleukin-6. In the case of HIC, the proteins were bound to a phenyl-Sepharose column in the presence of ammonium sulfate (AS) with or without arginine and eluted with a descending concentration of AS. While use of 1 M AS in the loading buffer resulted in complete binding of the mAb, inclusion of 1 M arginine in loading and equilibration buffer, only when using low-substituted phenyl-Sepharose, resulted in weaker binding of the proteins. While decreasing AS concentration to 0.75 M resulted in partial elution of the mAB, elution was facilitated with inclusion of 0.5-1 M arginine. In the case of IEC, arginine was included in the loading samples. Inclusion of arginine during binding to the IEC columns resulted in a greater recovery and less aggregation even when elution was done in the absence of arginine. These results indicate that arginine enhances elution of proteins bound to the resin, suggesting its effectiveness as a solvent for elution in HIC and IEC.     

Nuclear proteins. VI. Fractionation of chromosomal non-histone proteins using hydrophobic chromatography.

Mouse liver non-histone proteins, isolated by hydroxyapatite chromatography, were fractionated by hydrophobic chromatography using omega-amino-decyl-agarose omega-amino butyl-agarose, decyl-agarose, butyl-agarose, phenyl-Sepharose, and CPAD-Sepharose. Two column loading techniques were used. In the 0.35 M NaCl technique, the proteins were dialized into 0.35 M NaCl, applied to the column and initially eluted with 0.35 M NaCl. In the 40% (NH4)2SO4 technique, the non-histone proteins were mixed with the hydrophobic agarose, dialized against 40% (NH4)2SO4, and initially eluted with 40% (NH4)2SO4. In both cases the columns were subsequently eluted with 10 mM Tris-HCl, pH 7.5, 0.35, 1.0 and 5.0 M LiBr, and finally with 1% sodium dodecyl sulfate. The 0.35 M NaCl technique, using decyl-agarose and phenyl-Sepharose, resulted in a single step marked enrichment of the major hnRNA proteins (1 M LiBr fraction). The 40% (NH4)2SO4 technique resulted in a single step isolation of a pair of 15-20 000 dalton polypeptides.     

Purification of a cystic fibrosis plasmid vector for gene therapy using hydrophobic interaction chromatography

The success and validity of gene therapy and DNA vaccination in in vivo experiments and human clinical trials depend on the ability to produce large amounts of plasmid DNA according to defined specifications. A new method is described for the purification of a cystic fibrosis plasmid vector (pCF1-CFTR) of clinical grade, which includes an ammonium sulfate precipitation followed by hydrophobic interaction chromatography (HIC) using a Sepharose gel derivatized with 1,4-butanediol-diglycidylether. The use of HIC took advantage of the more hydrophobic character of single-stranded nucleic acid impurities as compared with double-stranded plasmid DNA. RNA, denatured genomic and plasmid DNAs, with large stretches of single strands, and lipopolysaccharides (LPS) that are more hydrophobic than supercoiled plasmid, were retained and separated from nonbinding plasmid DNA in a 14-cm HIC column. Anion-exchange HPLC analysis proved that >70% of the loaded plasmid was recovered after HIC. RNA and denatured plasmid in the final plasmid preparation were undetectable by agarose electrophoresis. Other impurities, such as host genomic DNA and LPS, were reduced to residual values with the HIC column (<6 ng/microg pDNA and 0.048 EU/microg pDNA, respectively). The total reduction in LPS load in the combined ammonium acetate precipitation and HIC was 400,000-fold. Host proteins were not detected in the final preparation by bicinchoninic acid (BCA) assay and sodium dodecylsulfate-polyacrylamide gel electrophoresis (SDS-PAGE) with silver staining. Plasmid identity was confirmed by restriction analysis and biological activity by transformation experiments. The process presented constitutes an advance over existing methodologies, is scaleable, and meets quality standards because it does not require the use of additives that usually pose a challenge to validation and raise regulatory concerns.     

Modeling of protein monomer/aggregate purification and separation using hydrophobic interaction chromatography

Hydrophobic interaction chromatography (HIC) is commonly used to separate protein monomer and aggregate species in the purification of protein therapeutics. Despite being used frequently, the HIC separation mechanism is quite complex and not well understood. In this paper, we examined the separation of a monomer and aggregate protein mixture using Phenyl Sepharose FF. The mechanisms of protein adsorption, desorption, and diffusion of the two species were evaluated using several experimental approaches to determine which processes controlled the separation. A chromatography model, which used homogeneous diffusion (to describe mass transfer) and a competitive Langmuir binary isotherm (to describe protein adsorption and desorption), was formulated and used to predict the separation of the monomer and aggregate species. The experimental studies showed a fraction of the aggregate species bound irreversibly to the adsorbent, which was a major factor governing the separation of the species. The model predictions showed inclusion of irreversible binding in the adsorption mechanism greatly improved the model predictions over a range of operating conditions. The model successfully predicted the separation performance of the adsorbent with the examined feed.