Multivalent interaction chromatography as exemplified by the adsorption and desorption of skeletal muscle enzymes on hydrophobic alkyl-agaroses

Hydrophobic interaction chromatography of proteins IV

Adsorption of proteins on surfaces of hydrophobic interaction chromatography media is at least a two-stage process. Application of pure protein pulses (bovine serum albumin and beta-lactoglobulin) to hydrophobic interaction chromatography media yielded two chromatographic peaks at low salt concentrations. At these salt concentrations, the adsorption process is affected by a second reaction, which can be interpreted as protein spreading or partial unfolding of the protein. The kinetic constants of the spreading reaction were derived from pulse response experiments at different residence times and varying concentrations by applying a modified adsorption model considering conformational changes. The obtained parameters were used to calculate uptake and breakthrough curves for spreading proteins. Although these parameters were determined at low saturation of the column, predictions of overloaded situations could match the experimental runs satisfactorily. Our findings suggest that proteins which are sensitive to conformational changes should be loaded at high salt concentrations in order to accelerate the adsorption reaction and to obtain steeper breakthrough curves.

Interaction of fibrinogen with n-alkylagaroses and its purification by critical hydrophobicity hydrophobic interaction chromatograpy

A rational application of hydrophobic interaction chromatography (HIC) to the purification of proteins has remained an enigma in spite of over 30 years of research. The critical hydrophobicity parameter, which can be determined from a concentration series of n-alkyl Sepharose 4B (Seph-Cn) offers the possibility of adapting the HIC gel to the needs of purification. To this end a library of HIC gels (Seph-C4 to Seph-C6) of different immobilized alkyl residue concentrations was synthesized and tested with purified bovine fibrinogen. Binding of fibrinogen to such a concentration series resulted in sigmoidal binding curves. Analysis of the Seph-C5 data according to the lattices-site binding model yielded adsorption coefficients (nS) between 5 and 10 indicating that 5-10 lattice-sites (alkyl residues) interact multivalently with a fibrinogen molecule for adsorption at low ionic strength. The apparent lattice-site half-saturation constant of dissociation lies between 21 and 25 micromol/ml packed gel. For each alkyl chain length a critical hydrophobicity could be determined. For fibrinogen purification the critical hydrohobicity gel, Seph-C5 (13 micromol/ml packed gel), was selected. With the help of the cosolvents NaCl or glycine a fully reversible adsorption of fibrinogen could be facilitated on the critical hydrophobicity gel. Application of the method to human and bovine blood plasma resulted in a single step purification of fibrinogen in high yields. A comparison of the classical purification of fibrinogen with the critical hydrophobicity HIC (CHIC) method demonstrates a reduction in preparation time from several days to ca. 1 h. The subunit structure of HIC-purified human fibrinogen is identical to the classically purified protein. In the case of bovine fibrinogen however HIC-purified fibrinogen displayed a different subunit structure in that the Aalpha chain of fibrinogen had a ca. 5 kDa higher molecular mass. This may be due to the rapidity of the new one-step method and an avoidance of proteolysis.

Modeling of the salt effects on hydrophobic adsorption equilibrium of protein

A two-state protein model is proposed to describe the salt effects on protein adsorption equilibrium on hydrophobic media. This model assumes that protein molecules exist in two equilibrium states in a salt solution, that is, hydrated and dehydrated states, and only the dehydrated-state protein can bind to hydrophobic ligands. In terms of the two-state protein hypothesis and the steric mass-action theory, protein adsorption equilibrium on hydrophobic media is formulated by a five-parameter equation. The model is demonstrated with the adsorption of bovine serum albumin to Phenyl Sepharose gels as a model system. The effects of salt type (sodium chloride, sodium sulfate and ammonium sulfate) on the model parameters are discussed. Then, the model formulism is simplified in terms of the small magnitude of the protein dehydration equilibrium constant in the model. This simplification has returned the model derived on the basis of the two-state protein hypothesis to its original mechanism of salt effects on the hydrophobic adsorption of protein. This simplified model also creates satisfactory prediction of protein adsorption isotherms.

Microcalorimetric studies of interactions between proteins and hydrophobic ligands in hydrophobic interaction chromatography: effects of ligand chain length, density and the amount of bound protein

Using isothermal titration calorimetry (ITC), this investigation directly measured the adsorption enthalpies of proteins on various hydrophobic adsorbents. Various amounts of butyl and octyl groups were attached onto CM-Sepharose to form C4 and C8, two types of hydrophobic adsorbents. The adsorption enthalpies of both trypsinogen and alpha-chymotrypsinogen A were measured at 4.0 M NaCl and pH 10.0, in which most ionic interaction was suppressed. The adsorption isotherms of both proteins on various adsorbents were also measured, thus allowing us to calculate the Gibbs free energy and entropy of adsorption. Experimental results indicated that the adsorption of both proteins on butyl-containing adsorbents was exothermic, while their adsorption on octyl ones was endothermic. In addition, binding of both proteins with the butyl ligand is basically an adsorption process, while binding with the octyl ligand is adsorption and partition processes. Moreover, on both butyl or octyl, the adsorption enthalpy became increasingly positive as the ligand density increased, while the adsorption entropy became more positive as the alkyl chain length or density of the adsorbent increased. In addition, ITC was used to measure protein-protein interaction. The adsorption enthalpy of both proteins increased as the amount of bound protein increased, and the enthalpy increase of trypsinogen appeared to be higher than that of alpha-chymotrypsinogen A. This observation implies that protein-protein repulsion was stronger among trypsinogen molecules in the experiments.

Hydrophobic charge induction chromatography: salt independent protein adsorption and facile elution with aqueous buffers

A new form of protein chromatography, hydrophobic charge induction, is described. Matrices prepared by attachment of weak acid and base ligands were uncharged at absorption pH. At low ligand densities, protein adsorption was typically promoted with lyotropic salts. At higher ligand densities, chymosin, chymotrypsinogen and lysozyme were adsorbed independently of ionic strength. A pH change released the electrostatic potential of the matrix and weakened hydrophobic interactions, inducing elution. Matrix hydrophobicity and titration range could be matched to protein requirements by ligand choice and density. Both adsorption and elution could be carried out within the pH 5-9 range.

Carbonic anhydrase in Acetobacterium woodii and other acetogenic bacteria

Acetobacterium woodii, Acetohalobium arabaticum, Clostridium formicoaceticum, and Sporomusa silvacetica were found to contain carbonic anhydrase (CA). Minimal to no CA activity was detected in Moorella thermoautotrophica, Moorella thermoacetica subsp. "pratumsolum," Sporomusa termitida, and Thermoanaerobacter kivui. Of the acetogens tested, A. woodii had the highest CA specific activity, approximately 14 U mg of protein(-1), in extracts of either glucose- or H2-CO2-cultivated cells. CA of A. woodii was cytoplasmic and was purified approximately 300-fold to a specific activity of 5,236 U mg of protein(-1). Intracellular acetate concentrations inhibited CA activity of A. woodii by 50 to 85%, indicating that intracellular acetate may affect in situ CA activity.

Unstable proteins: how to subject them to chromatographic separations for purification procedures

The chromatographic separation of an unstable protein is often a challenge to the scientist working in the field of life sciences. Especially for the purification of sensitive enzymes, making use of conventional chromatographic techniques is difficult and frequently results in a complete loss of biological activity of the target protein. This report summarizes some general strategies that may help to keep unstable proteins in their native conformation during the rather harsh conditions of a purification procedure. In this context, a recently developed hollow fiber membrane module, suitable for performing on-line dialysis, is introduced and examples of its application to liquid column chromatography are given. Many innovative separation techniques, characterized by dramatic improvements in both performance and separation time, have recently been developed. Since the chromatographic separation of unstable proteins requires the use of modern state-of-the-art equipment and technology, emphasis is given to newly developed separation techniques such as expanded bed adsorption, perfusion chromatography, protein free flow electrophoresis and the use of tentacle gels. In addition, examples of recently published purifications of unstable proteins are discussed with respect to strategies ensuring the preservation of the native protein structure during chromatographic separation.

Monitoring fibrinogen adsorption kinetics by interfacial TIRF rheometry

The adsorption kinetics of purified fibrinogen to unmodified and aminopropylsilane-modified quartz glass surfaces were studied under pseudo-first order (binding-unit excess) conditions by the total internal reflection fluorescence (TIRF) method. Fluorescence in the adsorbed protein layer (350 nm) was excited by the evanescent wave at 285-290 nm. In order to reduce and possibly eliminate the influence of mass transfer on the kinetics of fibrinogen adsorption, a novel protein adsorption chamber containing a cone-and-plate rheometer with total internal reflection technology was employed. The aim of the study was to obtain critical shear rates, at which the adsorption rate of fibrinogen became independent of diffusion. Therefore, shear rates were varied between 0 and 7200 s-1 at initial fibrinogen concentrations of c9 = 4.7 and 17.7 micrograms mL-1. The adsorption rate of fibrinogen increased 5-17-fold, depending on the surface, as the critical shear rate was approached. Above the critical shear rates the kinetic data of fibrinogen adsorption could be fitted at c9 = 4.7 micrograms mL-1 to a single exponential function, indicating the predominance of a single binding step with a half-life of ca 20 s. At the higher initial concentration of c9 = 17.7 micrograms/mL-, however, a significant deviation from the single exponential behavior was observed in the first 10 s of the adsorption reaction, indicating a very fast initial event with a half-life of ca 5 s in addition to a slower binding reaction with a half-life of ca 35 s. Thus the novel TIRF rheometer can resolve kinetics down to half-lives of 5 s and possibly even lower.

Multipoint binding in metal-affinity chromatography II. Effect of pH and imidazole on chromatographic retention of engineered histidine-containing cytochromes c

Protein binding in immobilized metal affinity chromatography (IMAC) was studied using a set of Saccharomyces cerevisiae iso-1-cytochrome c variants which differed only in their histidine content and placement. Elution with an imidazole gradient enabled separation of cytochrome c variants based on their histidine multiplicity. Millimolar concentrations of imidazole dramatically decreased protein partitioning to the IMAC support as measured by the chromatographic capacity factors under isocratic conditions. Fitting the partitioning data to the "stoichiometric displacement" model indicates that cytochrome c variants containing from one to four surface histidines each displaced approximately three equivalents of imidazole upon adsorption. Therefore even a protein with a single surface histidine appears to coordinate to multiple copper sites on the IMAC support at neutral pH. The effect of pH on the capacity factors of these variants measured in the absence of imidazole further supports this interpretation. Although the presence of a surface histidine was required for retention at neutral pH, a variant with no surface histidines still partitioned strongly to the IMAC support at higher pH (pH > 7.5). These results indicate the contribution of additional protein-metal-coordinating groups, presumably surface amines, to chromatographic retention in IMAC.

Base-atom recognition in protein adsorption to alkyl agaroses

The three proteins phosphorylase b, calmodulin and fibrinogen are adsorbed onto thioalkyl derivatives of Sepharose much more strongly than onto gels carrying the same alkyl residue coupled via a carbamate linkage. This enhancement of binding onto alkyl-S-Sepharoses compared with alkyl-N-agaroses is not primarily due to an increase in the extent of conformational changes of the proteins occurring on the gel surface. This can be shown in experiments with the tripeptide Trp-Trp-Trp. The Trp tripeptide is also adsorbed with a much higher affinity to butyl-S-Sepharose than to butyl-N-Sepharose, showing that the primary interaction between the immobilized alkyl residue and the amino acids of the protein is decisive for adsorption. A model stressing the strong influence of an atom or a group of atoms at the base of an immobilized alkyl residue is described as "base-atom recognition".

Rapid protein purification using phenylbutylamine-Eupergit: a novel method for large-scale procedures

Electrophoretic desorption was used to compare the protein binding capacities of some hydrophobic adsorbents [the phenylbutylamine (PBA) derivatives of Eupergit C and agarose and Phenyl-Sepharose] for low-pressure chromatography. The highest capacity was observed for the bifunctional adsorbent PBA-Eupergit. The hydrophobically adsorbed proteins can be selectively desorbed by decreasing the pH of the eluent due to electrostatic repulsion between positive charges on the adsorbed proteins and positively charged secondary amines on the adsorbent. This was used to purify 1500 U penicillin amidase from E. coli homogenates per gram wet weight of PBA-Eupergit in 50 adsorption-desorption cycles without organic solvents (greater than 90% yield, purification factor = 5.3).

Microbore flow-rates and protein chromatography

Reversed-phase chromatography of proteins on microbore columns can achieve sensitivities that exceed those for standard-bore columns by a factor of 10-20, when operated at the same linear velocities. These gains in sensitivity are accompanied by proportional reductions in peak volume. Sensitivities on standard- (4.6 mm I.D.) and narrow-bore (2.1 mm I.D.) columns have been further improved by reducing the flow-rates to those typical for microbore (1 mm I.D.) columns. We have investigated the role of flow-rate in determining peak volumes for a constant time gradient and found that flow-rate affects peak volume to a much greater extent than column diameter. Column length was not found to have a significant effect on either peak volume or sensitivity. We have found that a four-fold reduction in flow-rate results in at least a two-fold reduction in peak volume over the flow-rate range from 25 to 400 microliters/min. Recovery of proteins in smaller volumes should prove beneficial to subsequent protein characterization methodologies.

Multimodal liquid chromatography columns for the separation of proteins in either the anion-exchange or hydrophobic-interaction mode

Several high-performance stationary phases suitable for protein chromatography were synthesized. Columns packed with these materials could be operated independently in either the anion-exchange or hydrophobic-interaction mode. Two approaches were used to prepare these materials. In the first method, a polyamine was adsorbed on the surface of macroporous silica and then crosslinked with a multifunctional oxirane. The hydrophobicity of the crosslinking agent and the extent of interconnection were used to modulate the electrostatic and solvophobic interactions. The second approach also utilized a crosslinked polyamine stationary phase; however, the forces of interaction were attenuated through controlled acylation of surface amines with a small anhydride molecule. The resolving ability of these columns, functioning in either mode, was comparable to commercial high-performance liquid chromatographic columns, designed to operate by a single retention mechanism. Column selectivity for proteins was completely different in each mode. Protein fractions collected from a multimodal column, operated in the anion-exchange mode, could be further purified by rechromatographing them on the same column in the hydrophobic-interaction mode. Utility of the multimodal column was demonstrated with the fractionation of several cytochromes and ferredoxins from the cyanobacterium Microcystis aeruginosa.

Salt-promoted adsorption: recent developments

Efficient fractionation of human serum proteins is accomplished by use of a series of tandem-coupled beds of group-affinity adsorbents. The general fractionation strategy for group fractionation of a complex protein mixture is discussed.

High-performance liquid chromatography column length designed for submicrogram scale protein isolation

High-performance liquid chromatography of small amounts of protein was readdressed with respect to current gas-phase sequencing technology. Useful primary sequence information can be obtained from as little as 5-100 pmol of material. This corresponds on a mass level to the nanogram to microgram range where, unfortunately, HPLC columns often give low recoveries depending on the size and surface hydrophobicity of the peptide or protein. It was rationalized in this study that reduced column length could have a beneficial effect on recovery without significant loss of resolution. To demonstrate this, six HPLC columns ranging from 0.2 to 25 cm in length were made and evaluated in terms of protein loading and resolution. Column lengths of less than 1 cm were found to increase recovery of surface hydrophobic proteins without loss of resolution, as shown for a standard protein profile. These columns resolve proteins best when loaded with less than 10 micrograms, with recoveries greater than 90%. All column internal diameters were at least 4.1 mm so that standard HPLC pumps could be used to generate gradients.

Synthesis of new hydrophobic adsorbents based on homologous series of uncharged alkyl sulphide agarose derivatives

A homologous series of uncharged thioalkyl derivatives of agarose were prepared by a simplified synthetic route and their adsorption behaviour towards human serum proteins was evaluated and compared with that of a commercially available alkyl ether derivative of agarose. The influence of the spacer arm length on the adsorption efficiency was also investigated. The degree of substitution of the derivatives can be estimated conveniently by sulphur analysis. The four different types of thiolkyl derivatives (C6, C8, C12 and C14) investigated here behave in all respects like hydrophobic adsorbents. The coupling yield obtained is high (75% or more) and is better than that obtained by alternative synthetic routes reported so far. The adsorption capacity towards serum proteins of the various derivatives increases with increasing alkyl chain length and degree of substitution. Desorption is achieved by a progressive decrease in the polarity of the eluent and the recovery of the applied material is in the range 80-90%. The role played by the thioether as a possible modulator of the observed hydrophobic adsorption is discussed. For the group separation of serum proteins the optimum adsorbent, as regards capacity combined with ease of elution of adsorbed material, should be substituted with chains of six or eight carbon atoms and have a ligand concentration in the range 80-120 mumole g-1 dry gel.

Effects of urea-thermal denaturation on the high-performance cation-exchange chromatography of alpha-chymotrypsinogen-A

Retention parameters of alpha-chymotrypsinogen-A were determined by isocratic elution for a series of concentrations of calcium acetate and sodium acetate both in the presence and absence of urea. Under non-denaturing conditions of temperature and urea concentration, urea facilitated elution. Under reversible denaturing conditions a sharp drop in chromatographic retention was observed over a narrow temperature range which could be correlated with equilibrium measurements of the protein fluorescence. Retention of both native and denatured protein could be fit to a non-mechanistic retention model by plotting the log k' against log salt concentration. Conventional interpretation of these findings indicates that, while the number of ions displaced during binding is greater for the denatured protein, the affinity per ion decreases since the retention of denatured protein is much less than native. Elution profiles obtained under partially denaturing conditions showed a strong flow-rate dependence. We attribute these observations to a rate of equilibration between native and denatured protein that is on the timescale of the chromatographic rate processes.

Retention model for proteins in reversed-phase liquid chromatography

This paper presents a retention model for proteins on an reversed-phase chromatography support in which retention is a function of the number (Z) of solvent molecules required to displace the solute from the surface. An equation is derived that relates the capacity factor of a protein to the displacing agent concentration and the stoichiometry of solvent-solute displacement. Experimental tests of the model indicate that each protein has a unique Z value and that Z is directly proportional to the molecular weight of a series of proteins when 60% formic acid is used as the mobile phase additive. This relationship is attributed to a direct relationship between Z and the contact surface area between polypeptide solutes and the support. Desorption curves for proteins also become more convex with increasingly molecular weight, as predicted by the retention model. In the solvent series of methanol, ethanol, propanol, the Z number decreases from the C1 to C3 alcohol. The Z number for any particular solvent is also related to other mobile phase additives, such as acids, and the concentration of additives.

Mobile-phase and temperature effects in the reversed phase chromatographic separation of proteins

This paper explores the influence of mobile-phase and temperature effects on the gradient elution reversed phase chromatographic behavior of proteins. Using LiChrospher SI 500, bonded with n-butyl groups and a gradient in 1-propanol, 10 mM H3PO4, rapid separation and high mass recovery were obtained for a series of globular proteins. This protein separation and recovery are compared to those obtained when acetonitrile and acetonitrile plus 10 mM H3PO4 are used as eluting gradient solvents. In general, acetonitrile yielded lower recovery than 1-propanol, particularly for the more hydrophobic proteins, e.g., ovalbumin. For all three gradient solvents, little difference was observed in retention or recovery when the n-alkyl chain of the bonded phase varied. On the other hand, relative to the n-alkyl phases, a significantly lower retention of all proteins was found on more hydrophilic phases, e.g., cyano and nonendcapped n-butyl, when acetonitrile was the organic modifier, while in the case of 1-propanol, no retention difference was observed. Thus, column comparisons depend on the protein/mobile-phase combinations examined. The role of column temperature was also studied, and it was found that for certain proteins dramatic changes in peak shape occurred as a function of temperature. The influences of ionic strength and salt type were also studied. Protein mass recovery was shown to decrease with an increase in salt concentration; moreover, perchlorate was shown to have a larger effect in this regard than phosphate. In addition, salt concentration and type were found to influence peak shape greatly in certain cases. The results indicate the strong influences of mobile phase and temperature on chromatographic behavior, and some of the options available when this behavior is not satisfactory. Several protein separations are presented illustrating the power of the reversed phase approach.

High-performance liquid chromatography of biopolymers

The ability to separate biological macromolecules with good resolution on liquid chromatographic columns has depended on the development of suitable packing materials. In size exclusion chromatography, molecules are separated by size on the basis of differential permeation of the packing. Ion exchange, hydrophobic interaction (or reversed-phase), and affinity chromatography are all surface-mediated separation methods, although they depend on different retention mechanisms. High-performance liquid chromatographic columns designed for biopolymers offer major advantages over conventional columns in both speed and resolving power. The exponential growth of literature on the high-performance separation of peptides and proteins in particular indicates that the technique will become the dominant form of column liquid chromatography.