Bioluminescence assay for estimating the hydrophobic properties of bacteria as revealed by hydrophobic interaction chromatography.

The luciferin-luciferase bioluminescence method was used to estimate the number of bacteria retained in neutral and amphiphilic gels and those in the eluate to determine the hydrophobic surface properties of bacteria by using hydrophobic interaction chromatography. Good correlations were found between viable counts and ATP content for Escherichia coli, Pseudomonas fragi, and Listeria monocytogenes. ATP determination was more rapid than viable counts for characterizing the relative hydrophobicity of L. monocytogenes. Quantitative estimations of adsorption of L. monocytogenes on octyl-Sepharose indicate that this microorganism is hydrophilic.     

High surface hydrophobicity ofStaphylococcus aureus as revealed by hydrophobic interaction chromatography

Hydrophobic interaction chromatography (HIC) on Octyl Sepharose^R in a column procedure was used to compare the relative surface hydrophobicity ofStaphylococcus aureus reference strains, protein A-negative mutants, and strains isolated from bovine mastitis. High protein A-producing strains (Cowan 1 and clinical isolate SA 17970) showed a higher relative surface hydrophobicity than did strains producing a low amount of protein A. One encapsulatedS. aureus strain (Smith diffuse) did not bind to the gel, while an unencapsulated variant showed binding properties similar to weak protein A-producing strains. Studies onS. aureus strains isolated from bovine mastitis revealed a good correlation between adsorption to Octyl Sepharose and the production of protein A. Results indicate that protein A and probably other surface proteins such as fibronectin-binding protein contribute to the high relative surface hydrophobicity ofS. aureus.     

Purification and fractionation of lipopolysaccharide from gram-negative bacteria by hydrophobic interaction chromatography

By hydrophobic interaction chromatography on octyl-Sepharose, lipopolysaccharide (LPS) of Escherichia coli Re mutant and of wild-type smooth-form (S-form) Salmonella typhimurium and Salmonella abortus equi is fractionated according to increasing amount of fatty acids. Thereby a fractionation of S-form LPS according to the length of the O-polysaccharide chain also occurs, because with increasing of fatty acids there is a decrease in the mean length of the O-polysaccharide chain from approximately 30 to 4 repeating units. Molecular species of Re-mutant LPS contain four 3-hydroxytetradecanoyl residues in addition to which dodecanoic, tetradecanoic and possibly hexadecanoic acid, appear in this sequence. Among the molecular species of S-form LPS, dodecanoic, tetradecanoic and hexadecanoic acids appear in the same order, but in contrast to Re-mutant LPS a significant fraction of S-form LPS contains less than four 3-hydroxytetradecanoyl residues. Hydrophobic interaction chromatography also proved an effective one-step purification procedure of LPS as was shown with a crude preparation from S-form S. typhimurium.     

Evaluation of modified chitosan as matrix for hydrophobic interaction chromatography

Chitosan beads were modified with glutaraldehyde and modified chitosan was investigated as matrix for hydrophobic interaction chromatography. The influence of temperature, type of salt and its ionic strength on the adsorption of -galactosidase was studied. -Galactosidase was found to bind in presence of high concentration of ammonium sulphate (3 M, w/v) and 90% of the bound enzyme was eluted with decreasing salt concentration in presence of 10% ethylene glycol. Attempt was made to purify -galactosidase from modified chitosan, -galactosidase showed 1.7-fold purification with 43.96% recovery of enzyme activity. The SDS–PAGE analysis of enzyme showed considerable purification and its molecular weight was found to be 63–64 kDa. Unlike other chromatographic matrices, the prepared chitosan beads were used five times. The results showed that purification and recovery of the enzyme did not change even when column size was increased.     

An alternative assay to hydrophobic interaction chromatography for high-throughput characterization of monoclonal antibodies

The effectiveness of therapeutic monoclonal antibodies (mAbs) is governed not only by their bioactivity, but also by their biophysical properties. Assays for rapidly evaluating the biophysical properties of mAbs are valuable for identifying those most likely to exhibit superior properties such as high solubility, low viscosity and slow serum clearance. Analytical hydrophobic interaction chromatography (HIC), which is performed at high salt concentrations to enhance hydrophobic interactions, is an attractive assay for identifying mAbs with low hydrophobicity. However, this assay is low throughput and thus not amenable to processing the large numbers of mAbs that are commonly generated during antibody discovery. Therefore, we investigated whether an alternative, higher throughput, assay could be developed that is based on evaluating antibody self-association at high salt concentrations using affinity-capture self-interaction nanoparticle spectroscopy (AC-SINS). Our approach is to coat gold nanoparticles with polyclonal anti-human antibodies, use these conjugates to immobilize human mAbs, and evaluate mAb self-interactions by measuring the plasmon wavelengths of the antibody conjugates as a function of ammonium sulfate concentration. We find that hydrophobic mAbs, as identified by HIC, generally show significant self-association at low to moderate ammonium sulfate concentrations, while hydrophilic mAbs typically show self-association only at high ammonium sulfate concentrations. The correlation between AC-SINS and HIC measurements suggests that our assay, which can evaluate tens to hundreds of mAbs in a parallel manner and requires only small (microgram) amounts of antibody, will enable early identification of mAb candidates with low hydrophobicity and improved biophysical properties.     

An alternative assay to hydrophobic interaction chromatography for high-throughput characterization of monoclonal antibodies

The effectiveness of therapeutic monoclonal antibodies (mAbs) is governed not only by their bioactivity, but also by their biophysical properties. Assays for rapidly evaluating the biophysical properties of mAbs are valuable for identifying those most likely to exhibit superior properties such as high solubility, low viscosity and slow serum clearance. Analytical hydrophobic interaction chromatography (HIC), which is performed at high salt concentrations to enhance hydrophobic interactions, is an attractive assay for identifying mAbs with low hydrophobicity. However, this assay is low throughput and thus not amenable to processing the large numbers of mAbs that are commonly generated during antibody discovery. Therefore, we investigated whether an alternative, higher throughput, assay could be developed that is based on evaluating antibody self-association at high salt concentrations using affinity-capture self-interaction nanoparticle spectroscopy (AC-SINS). Our approach is to coat gold nanoparticles with polyclonal anti-human antibodies, use these conjugates to immobilize human mAbs, and evaluate mAb self-interactions by measuring the plasmon wavelengths of the antibody conjugates as a function of ammonium sulfate concentration. We find that hydrophobic mAbs, as identified by HIC, generally show significant self-association at low to moderate ammonium sulfate concentrations, while hydrophilic mAbs typically show self-association only at high ammonium sulfate concentrations. The correlation between AC-SINS and HIC measurements suggests that our assay, which can evaluate tens to hundreds of mAbs in a parallel manner and requires only small (microgram) amounts of antibody, will enable early identification of mAb candidates with low hydrophobicity and improved biophysical properties.     

Purification of factor X by hydrophobic interaction chromatography

Human factor X has been purified to homogeneity by hydrophobic interaction chromatography on phenyl-sepharose. The coagulation protein did not interact with the resin in the presence of 2–3 M NaCl whereas contaminants were retained. This single purification step, in conjunction with classical purification strategies, is a powerful tool in generating high purity factor X and is based on resins which are readily available.     

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.     

Fractionation of non allelic histone variants by hydrophobic interaction chromatography

A method for the separation of non allelic histone variants is described. Sepharose-CL-4B was modified with dodecylamine by the carbonyldiimidazole-method. The matrix prepared contained 6 mumol/ml hydrophobic groups, C12-hydrocarbon chains. Proteins were loaded at high ionic strength and eluted from the column with an urea gradient. Histones H1, H2a and H2b from different mammalian tissues were loaded on the column and pure variants H1A, H1B, H2a1, H2a2, H2b1 and H2b2 were obtained by urea gradient elution. The recovery of the H2a-variants from calf thymus for example was 54% of H2a1 and 36% of H2a2.     

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.     

Fractionation of avian erythrocyte histones by hydrophobic interaction chromatography.

The interactions of H1 (H1A, H1B), H2A, H2B, H3, H4, and H5 with phenyl cross-linked agarose were studied. Procedures are described whereby all six histones can be bound, released, and fractionated by using appropriate salt concentrations or pH. The binding can be totally abolished by inclusion of hydrophobic disrupting agents. Control experiments with nonderivated cross-linked agarose ruled out a passive aggregation-disaggregation phenomenon governing the binding patterns. The absorption sequence based on the identification and quantitation of individual histones from either unfractionated (whole) histone or separate histone classes is as follows: H3 greater than or equal to H4 greater than H2B greater than or equal to H5 greater than or equal to H2A greater than H1A greater than or equal to H1B. The order differs only slightly from the reverse of the desorption sequence, H1B less than or equal to H1A less than or equal to H5 less than H2A less than or equal to H3. Preferential interaction of H2A-H2B, H3-H4, and H2A-H2B-H4 occur; these interactions can modify the original relative affinity of each individual component for the matrix. The variability in matrix affinity appears to involve simple stoichiometry of the histone components.     

Rapid desalting of ammonium sulfate solutions by hydrophobic interaction chromatography

Open-air hydrophobic interaction chromatography with alkyl carbon functional groups coupled to agarose beads has been used to desalt large volumes of ammonium sulfate-fractionated bacterial cell lysates. The protein of interest can be simultaneously desalted and concentrated in less than 4 h, and the yield is significantly better than that obtained by the standard technique of precipitation, centrifugation, and dialysis.     

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.     

Purification of human plasma retinol-binding protein by hydrophobic interaction chromatography

Human plasma retinol-binding protein has been purified to homogeneity by a simple method that requires an ammonium sulfate fractionation, a hydrophobic interaction chromatography on phenyl-Sepharose, which dissociates the complex between retinol-binding protein and its carrier, transthyretin, and a gel filtration on Sephadex G-50. The yield of pure protein is comparable or higher than that obtained with the more complex procedures previously reported.     

Purification of carbonic anhydrase isoenzymes by high-performance affinity chromatography and hydrophobic interaction chromatography

Isoenzymes of carbonic anhydrase were purified by a combination of affinity chromatography and hydrophobic interaction chromatography. Immobilization of sulfonamides on an epoxy-activated support provided a stationary phase for affinity chromatography which was stable to hydrolysis by carbonic anhydrase. A first purification step allowed the isolation of enzymes directly from homogenates of human erythrocytes and rat stomach. Without any further preparation, except the addition of ammonium sulfate to the eluate from affinity chromatography, the isoenzymes could be separated by hydrophobic interaction chromatography with very high recovery of protein and retention of enzymatic activity.     

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.     

Purification of monoclonal antibodies by hydrophobic interaction chromatography under no-salt conditions

Hydrophobic interaction chromatography (HIC) is commonly used as a polishing step in monoclonal antibody purification processes. HIC offers an orthogonal selectivity to ion exchange chromatography and can be an effective step for aggregate clearance and host cell protein reduction. HIC, however, suffers from the limitation of use of high concentrations of kosmotropic salts to achieve the desired separation. These salts often pose a disposal concern in manufacturing facilities and at times can cause precipitation of the product. Here, we report an unconventional way of operating HIC in the flowthrough (FT) mode with no kosmotropic salt in the mobile phase. A very hydrophobic resin is selected as the stationary phase and the pH of the mobile phase is modulated to achieve the required selectivity. Under the pH conditions tested (pH 6.0 and below), antibodies typically become positively charged, which has an effect on its polarity and overall surface hydrophobicity. Optimum pH conditions were chosen under which the antibody product of interest flowed through while impurities such as aggregates and host cell proteins bound to the column. This strategy was tested with a panel of antibodies with varying pI and surface hydrophobicity. Performance was comparable to that observed using conventional HIC conditions with high salt.     

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.     

Refolding and purification of interferon-gamma in industry by hydrophobic interaction chromatography

A new technology for renaturation with simultaneous purification of the recombinant human interferon-gamma (rhIFN-gamma) in downstream of biotechnology is presented. The strategies to develop the new technology in industry scale were suggested. Based on chemical equilibrium and molecular interactions, the principle of rhIFN-gamma refolding by HPHIC was described. The kind of stationary and mobile phases were evaluated and found the former to contribute to the rhIFN-gamma refolding more than the latter. The extract containing the rhIFN-gamma in gram scale in 7.0 mol L(-1) guanidine hydrochloride solution of 700 mL was directly pumped into a unit of simultaneous renaturation and purification of proteins (USRPP, 10 x 300 mm i.d.) packed by small particle packings of hydrophobic interaction chromatography and a satisfactory recovery of bioactivity and mass of the rhIFN-gamma was obtained. With flow rate 100 mL min(-1) and a gradient elution by only one step in 4h, the purity and specific bioactivity approach to 95% and 8.7 x 10(7) IU(-1) mg, respectively. To evaluate the goodness of the presented new technology in this study, a usual method with the renaturation by dilution method firstly and then purification with a series of LC in literature was employed to compare with each other. The obtained result in terms of purity, recoveries of mass and bioactivity, cost time as well as expenses, the former is much better than the latter. Comparing the total bioactivity of rhIFN-gamma in the extract before to that after the renaturation by the USRPP, the total bioactivity of rhIFN-gamma increased 62-fold.     

Optimal operation conditions for protein separation in hydrophobic interaction chromatography

Protein retention in hydrophobic interaction chromatography is determined by protein physicochemical properties and by system characteristics. In this paper we present an attempt to determine the optimal operation conditions that would allow the separation of binary protein mixtures. The statistically significant system variables were determined, and then empirical models were obtained which explained more than 92% of variability in dimensionless retention time based on salt properties, ionic strength of the initial eluent and substitution degree of the resin. These variables were optimized in order to achieve the maximum retention time difference between two proteins in a mixture. The optimum operation conditions as predicted by the models were tested experimentally, showing a good agreement with predicted separation. We concluded that it would be possible to determine the system conditions that allow the maximum separation of two proteins based on the main system properties. The methodology proposed here presents potential to be applied to partially characterized systems, however, it could be improved if protein's properties were included explicitly in the models.