The influence of grafted polymer architecture and fluid hydrodynamics on protein separation by entropic interaction chromatography

Entropic interaction chromatography (EIC) provides efficient size-based separation of protein mixtures through the entropy change associated with solute partitioning into a layer of hydrophilic homopolymer that has been end-grafted within the pores of a macroporous chromatography support. In this work, surface-initiated atom-transfer radical polymerization (ATRP) is used to prepare a library of EIC stationary phases covering a wide range of grafted-chain densities and molecular weights. Exhaustive chain cleavage and analysis by saponification and GPC-MALLS, respectively, show that the new ATRP synthesis procedure allows for excellent control over graft molecular weight and polydispersity. The method is used to prepare high-density grafts (up to 0.164 +/- 0.005 chains/nm(2)) that extend the range of EIC applications to include efficient buffer-exchange and desalting of protein preparations. Reducing the graft density allows for greater partitioning of high molecular weight solutes, extending the linear range of the selectivity curve. Increasing graft molecular weight also alters selectivity, but more directly affects column capacity by increasing the volume of the grafted layer. Protein partitioning in high-density EIC columns is found to decrease with mobile-phase velocity (u). Although solute mass transfer resistances leading to an increase in plate height can explain this effect, pressure drop data across the column are indicative of weak convective flow through at least a fraction of the grafted architecture. Modeling of the grafted brush properties in the presence of solvent flow by subjecting a self-consistent-field theory representation of the brush to a viscous shear force predicts that the grafted chains will tilt and elongate in the direction of flow. The shear force may therefore act to reduce the number of conformations available to chains, increasing their rigidity without significantly altering the thickness of the grafted layer. A reduction in protein partitioning is then predicted when the dependence on u of the solute entropy loss is stronger than that of the grafted polymer, a condition met at high graft densities.     

Hydraulic characteristics of aerobic granules using size exclusion chromatography

Elution of poly(ethylene glycol) of molecular weight 200-20,000 Da from a size exclusion chromatography column packed with phenol-fed aerobic granules of three different nominal sizes (types I-III) has been investigated. The pore sizes of the three types of granules were evaluated based on the mean hydraulic times of the elution curves that decreased directly proportional to the increased logarithm of the molecular mass of a standard tracer and increased as granule size decreased. The corresponding exclusion limits for types I-III granules were 139,000, 123,000, and 54,500 Da, respectively. A one-dimensional convection-dispersion model described the effective dispersion coefficients of the tracers through the granule column. The intra-granular permeabilities and convective and diffusional transit times through the granule interior were evaluated by a dual porosity model. For small molecules of molecular mass <5,000 Da, intra-granular convection dominated transport mechanisms at fast moving velocity. For comparatively larger molecules, diffusion barrier existed to limit nutrient supply to the granules. The size exclusion test provided intra granular transport characteristics using detailed analysis on the elution data.     

Multidimensional profiling of plasma lipoproteins by size exclusion chromatography followed by reverse-phase protein arrays

The composition of lipoproteins and the association of proteins with various particles are of much interest in the context of cardiovascular disease. Here, we describe a technique for the multidimensional analysis of lipoproteins and their associated apolipoproteins. Plasma is separated by size exclusion chromatography (SEC), and fractions are analyzed by reverse-phase arrays. SEC fractions are spotted on nitrocellulose slides and incubated with different antibodies against individual apolipoproteins or antibodies against various apolipoproteins. In this way, tens of analytes can be measured simultaneously in 100 μl of plasma from a single SEC separation. This methodology is particularly suited to simultaneous analysis of multiple proteins that may change their distribution to lipoproteins or alter their conformation, depending on factors that influence circulating lipoprotein size or composition. We observed changes in the distribution of exchangeable apolipoproteins following addition of recombinant apolipoproteins or interaction with exogenous compounds. While the cholesteryl ester transfer protein (CETP)-dependent formation of pre-β-HDL was inhibited by the CETP inhibitors torcetrapib and anacetrapib, it was not reduced by the CETP modulator dalcetrapib. This finding was elucidated using this technique.     

On the use of mild hydrophobic interaction chromatography for "method scouting" protein purification strategies in aqueous two-phase systems: a study using model proteins

The behavior of a series of pure proteins partitioned in aqueous two-phase systems is compared with their behavior during mild hydrophobic interaction chromatography (HIC). A simple theoretical rationale for this comparison is presented based upon solvophobic theory. Similarities were found in the behavior of the model proteins in the two forms of partition chromatography. This indicates that HIC may be employed as a rapid instrumental technique for the broad characterization of protein behavior, which may be of benefit in the development of liquid-liquid partitioning strategies. However, it has proved difficult to completely account for this behavior on the basis of the known physical and structural properties of the proteins used. The variety in the detailed partitioning behavior of this small sample of protein types suggests that partition in aqueous two-phase systems is uniquely sensitive to subtle differences in surface properties of complex macromolecules. (c) 1994 John Wiley & Sons, Inc.     

On-line recovery of large molecules from mixtures using reciprocating size exclusion chromatography

Blue Dextran, a standard large molecule, was successfully recovered on-line from the aqueous mixture solution with nickel nitrate using a novel reciprocating size exclusion chromatography. After 7 cycles of repeating operations of frontal mode, 70% of Blue Dextran in the feed was isolated as a pure solution. On-line recovery of large molecules from the mixture is an unusual trial, comparing to the routine practice of filtration where small molecule is isolated from the mixture.     

Evaluation of exosome loading characteristics in their purification via a glycerol-assisted hydrophobic interaction chromatography method on a polyester,capillary-channeled polymer fiber phase

Exosomes are membrane-secreted vesicles, with sizes ranging from 30 to 150 nm, which play key roles in intercellular communication. There is intense interest in developing methods to isolate and quantify exosomes toward clinical diagnostics, fundamental studies of intercellular processes, and use of exosomes as delivery vehicles for therapeutic agents. Current methods for exosomes isolation and quantification are time consuming and have operational high costs; few combine isolation and quantification into a singular operation unit. This report describes the use of hydrophobic interaction chromatography on a polyester capillary-channeled polymer fiber column, employing a step gradient for exosome elution, including use of glycerol as a solvent modifier. The entire procedure is completed in 8 min, while maintaining the structural integrity and biological activity of the isolated exosomes. Electron microscopy was used to verify the size and structural fidelity of single exosomes. Absorbance response curves for a commercial exosome sample were used for exosome quantification in the chromatographic separations. In order to determine the dynamic loading capacity for exosomes, different volumes of Dictyostelium discoideum cell culture milieu supernatant were loaded at different column lengths (5–30 cm) and loading flow rates (0.2–0.5 ml/min). A loading capacity of 5.4 × 10¹² exosomes derived from D. discoideum milieu was obtained on a 0.8 × 300 mm column; yielding recoveries of over 80%. It is believed that this isolation and purification strategy holds many advantages toward the use of exosomes across a wide breadth of medical and biotechnology applications.     

Charaterization and hydrodynamic behaviour of modified gelatin: II. Characterization by high performance size exclusion chromatography — comparison with dextrans and proteins

Gelatin samples obtained by chemical modification (succinylation) are studied by SEC on silica based chromatographic supports. The influence of the pH of eluent mixtures (potassium phosphate added to NaCl) in the range 7-3.3 shows that the void volume peak (VVP) is lowered or even vanishes at pH 3.3 with the 3000 SW (TSK) gel. A process using an ultrasound treatment before injection is reported in order to determine accurately the molecular parameters of gelatin onto TSK gel with a minimal VV P. This peak is attributed to molecular aggregation of a part of the modified gelatin. After disaggregation by ultrasound or heat treatment the results are in good accordance with those obtained by other methods. It is demonstrated that with proteins and dextrans the TSK 3000 SW gel does not agree with the universal calibration curve (log[ν] · versus K_d as reported previously. A single calibration curve is obtained when the Stokes radius is plotted versus K_d. Gelatin fractions are eluted at pH 7 close to this calibration curve. This plot shows that gelatin fractions at pH 3.3 are not eluted by a pure size exclusion mechanism on 3000 SW gel. It is concluded that hydrophobic interactions between fractions of gelatin and the gel explain the high retention of these samples.     

On-line recovery of large molecules and concentration of small molecules using reciprocating size exclusion chromatography with temperature swing

The reciprocating size exclusion chromatography (RSEC) was operated with swing between two temperatures in a synchronous way with flow direction to recover a large solute on-line from the mixture, in addition to the small solute concentration. The concentration of small solutes in RSEC with a temperature swing was made possible by taking advantage of the temperature-dependent swelling properties of the porous gel. After 7 cycles of frontal mode operation, 76% of Blue Dextran in the feed was recovered and nickel nitrate in the feed reservoir was concentrated by 13%.     

Analytical characterization of a monoclonal antibody therapeutic reveals a three-light chain species that is efficiently removed using hydrophobic interaction chromatography

Size exclusion high performance liquid chromatography analysis of a human monoclonal antibody (mAb) showed the presence of a new species that eluted with a retention time between the dimeric and monomeric species of the antibody. Extensive characterization of this species, referred to as “shoulder,” indicated that it was a mAb containing an extra light chain and had a molecular weight of approximately 175 kDa. The extra light chain was found to be non-covalently associated with the Fab portion of the protein. The relative amount of shoulder (typically 1−3% of the total mAb present) varied with the Chinese hamster ovary cell line producing the mAb and was not influenced by the growth conditions. Our three-step mAb purification platform using protein A, anion exchange, and cation exchange process steps was successful at removing dimer and higher and lower molecular weight species, but not the shoulder impurity. It was found that hydrophobic interaction chromatography could be used in place of cation exchange to exploit the subtle differences in hydrophobicity between monomer and shoulder. We developed an antibody polishing process using Butyl Sepharose HP resin that is capable of removing the majority of high and low molecular weight impurities yielding 99% pure mAb monomer, virtually devoid of the shoulder species, with a step recovery of about 80%.     

On-line separation of solute mixtures using reciprocating size exclusion chromatography

Solutes of different size in a mixture solution were separated on-line, using a semi-continuous reciprocating size exclusion chromatography. The band of fast-moving large molecules was isolated during the first half cycle, while the band of slow-moving small molecules was isolated during the second half cycle. After 7 cycles of frontal mode operation, 89% of the Blue Dextran in the feed was isolated as a pure solution. Vitamin B₁₂ of constant concentration was also isolated as a pure solution.     

凝胶过滤层析参数对家蝇蛋白粗提液分离效果的影响

考察了凝胶过滤介质、层析柱直径、柱床高度和洗脱流速对家蝇Muscadomestica蛋白粗提液分离效果的影响,结果表明：凝胶过滤介质种类、层析柱直径、柱床高度、洗脱流速均能不同程度地影响家蝇蛋白粗提液的分离效果。在实验范围内,选择1.3 cm直径、40 cm柱床高度的Sephadex G-75,以0.4 mL/min的流速洗脱时,对家蝇蛋白粗提液的分离效果比较理想。     

Routine manufacture of recombinant proteins using expanded bed adsorption chromatography

Two different recombinant human proteins were purified directly from Pichia pastoris whole cell fermentation broth, containing 30–44% biomass (wet weight percent), by strong cation exchange expanded bed adsorption chromatography. Expanded bed adsorption chromatography provided clarification, product purification and product concentration in a single unit operation at large scale (2000-l nominal fermentation volume). The efficiency of expanded bed adsorption chromatography resulted in a short process time, high process yield, and limited proteolytic degradation of the target proteins. The separations were operated using a 60-cm (d) column run at 14 l/min. For one protein, expanded bed adsorption chromatography resulted in an average product recovery of 113% (relative to fermentation supernatant) and a purity of 89% (n=10). For the other protein, the average product recovery was 99% (relative to fermentation supernatant) and the purity was 62.1 (n=10). Laboratory experiments showed that biomass reduced product dynamic binding capacity for protein 2.     

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.     

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.     

Paper-PEG-based membranes for hydrophobic interaction chromatography: purification of monoclonal antibody

This article discusses the preparation of novel Paper-PEG interpenetrating polymer network-based membranes as inexpensive alternative to currently available adsorptive membranes. The Paper-PEG membranes were developed for carrying out hydrophobic interaction membrane chromatography (HIMC). PEG is normally very hydrophilic but can undergo phase separation and become hydrophobic in the presence of high antichaotropic salt concentrations. Two variants of the Paper-PEG membranes, Paper-PEG 1 and Paper-PEG 2 were prepared by grafting different amounts of the polymer on filter paper and these were tested for their hydraulic properties and antibody binding capacity. The better of the two membranes (Paper-PEG 1) was then used for purifying the monoclonal antibody hIgG1-CD4 from simulated mammalian cell culture supernatant. The processing conditions required for purification were systematically optimized. The dynamic antibody binding capacity of the Paper-PEG 1 membrane was about 9 mg/mL of bed volume. A single step membrane chromatographic process using Paper-PEG 1 membrane gave high monoclonal antibody purity and recovery. The hydraulic permeability of the paper-based membrane was high and was maintained even after many runs, indicating that membrane fouling was negligible and the membrane was largely incompressible.     

High-performance molecular sieve chromatography of proteins on agarose columns: the relation between concentration and porosity of the gel

Curves showing the relation between log (molecular weight) and distribution coefficient are presented for proteins subjected to molecular sieve chromatography on crosslinked and non-crosslinked agarose gels of different concentrations. These curves, which facilitate selection of the gel concentration that gives optimal resolution in any particular separation problem, show that the exclusion limit of 5, 9, 12, and 20% agarose gels correspond to protein with molecular weights above 1,000,000, 600,000, 450,000, and 280,000, respectively. Plate numbers have been determined for columns of 20% agarose at different flow rates and bead sizes. Separations of model proteins by high-performance molecular sieve chromatography on agarose beads are shown.     

A simple and rapid method for evaluation of Mark–Houwink–Sakurada constants of linear random coil polysaccharides using molecular weight and intrinsic viscosity determined by high performance size exclusion chromatography: application to guar galactomannan

A rapid method for establishing the constants in the Mark–Houwink–Sakurada equation, relating intrinsic viscosity and molecular weight (MW), of guar galactomannan is described. Following partial acid hydrolysis, the galactomannan was analyzed using high performance size exclusion chromatography employing viscosimetry and right angle light scattering detectors. In this way, a large number of samples of polysaccharides with a wide range of MW distributions were prepared, without need for isolation, and intrinsic viscosity and MW rapidly determined. The a and K values found for guar galactomannan were 0.72 and 5.13×10⁻⁴ ([η] in dl/g) respectively, in good agreement with previously published values.     

Technical note: Removal of metal ion inhibition encountered during DNA extraction and amplification of copper‐preserved archaeological bone using size exclusion chromatography

A novel technique for the removal of metal ions inhibiting DNA extraction and PCR of archaeological bone extracts is presented using size exclusion chromatography. Two case studies, involving copper inhibition, demonstrate the effective removal of metal ion inhibition. Light microscopy, SEM, elemental analysis, and genetic analysis were used to demonstrate the effective removal of metal ions from samples that previously exhibited molecular inhibition. This research identifies that copper can cause inhibition of DNA polymerase during DNA amplification. The use of size exclusion chromatography as an additional purification step before DNA amplification from degraded bone samples successfully removes metal ions and other inhibitors, for the analysis of archaeological bone. The biochemistry of inhibition is explored through chemical and enzymatic extraction methodology on archaeological material. We demonstrate a simple purification technique that provides a high yield of purified DNA (>95%) that can be used to address most types of inhibition commonly associated with the analysis of degraded archaeological and forensic samples. We present a new opportunity for the molecular analysis of archaeological samples preserved in the presence of metal ions, such as copper, which have previously yielded no DNA results. Am J Phys Anthropol, 2009. © 2009 Wiley‐Liss, Inc.     

Purification of recombinant aprotinin from transgenic corn germ fraction using ion exchange and hydrophobic interaction chromatography

Plants have attracted interest as hosts for protein expression because of the promise of a large production capacity and a low production cost. However, recovery costs remain a challenge as illustrated for recovery of recombinant aprotinin, a trypsin inhibitor, with removal of native corn trypsin inhibitor from transgenic corn (Azzoni et al. in Biotechnol Bioeng 80:268–276, 2002). When expression is targeted to corn grain fractions, dry milling can separate germ and endosperm fractions. Hence, only the product-containing fraction needs to be extracted, reducing the cost of extraction and the impurity level of the extract. Selective extraction conditions can reduce impurity levels to the point that low-cost adsorbents can result in relatively high purity levels. In this work, we attempted to achieve comparable purity with these lower cost methods. We replaced whole grain extraction and purification of recombinant aprotinin with sequential trypsin affinity and IMAC steps with an alternative of germ fraction extraction and purification with ion exchange and hydrophobic interaction chromatography (HIC). Using germ extraction at acidic pH supplemented with heat precipitation to remove additional host proteins resulted in a higher specific activity feed to the chromatographic steps. The cation exchange step provided 7.6× purification with 76.4% yield and no sodium dodecyl sulfate–polyacrylamide gel electrophoresis detectable native corn trypsin inhibitor. After the HIC step (2.7× step purification with 44.0% yield), the final product had a specific activity that was 75.3% of that of the affinity-purified aprotinin.