Productivity and operating regimes in protein chromatography using low-molecular-mass displacers

Sample displacement chromatography as a method for purification of proteins and peptides from complex mixtures

Sample displacement chromatography (SDC) in reversed-phase and ion-exchange modes was introduced approximately twenty years ago. This method takes advantage of relative binding affinities of components in a sample mixture. During loading, there is a competition among different sample components for the sorption on the surface of the stationary phase. SDC was first used for the preparative purification of proteins. Later, it was demonstrated that this kind of chromatography can also be performed in ion-exchange, affinity and hydrophobic-interaction mode. It has also been shown that SDC can be performed on monoliths and membrane-based supports in both analytical and preparative scale. Recently, SDC in ion-exchange and hydrophobic interaction mode was also employed successfully for the removal of trace proteins from monoclonal antibody preparations and for the enrichment of low abundance proteins from human plasma. In this review, the principals of SDC are introduced, and the potential for separation of proteins and peptides in micro-analytical, analytical and preparative scale is discussed.

Detection of trace proteins in multicomponent mixtures using displacement chromatography

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

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

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

Influence of pH and Ionic Strength on the Steric Mass-Action Model Parameters around the Isoelectric Point of Protein

The ion-exchange equilibrium and the dependence of the parameters in the steric mass-action (SMA) model on salt concentration and buffer pH around the isoelectric point of protein were studied. Bovine serum albumin (BSA, isoelectric point = 5.4) was used as a model protein and DEAE Sepharose FF as an ion exchanger. Finite batch adsorption experiments and isocratic elution chromatography were performed for the determination of the model parameters (i.e., characteristic charge, equilibrium constant, and steric factor). The results showed that pH had significant effects on the parameters. With an increase of pH from 4.5 to 6.5, the characteristic charge increased from 0.9 to 3.0 and leveled off as a plateau at pH above 5.5. The charge groups in the contact region of protein surface were considered to play a crucial role on the characteristic charge. The decrease of pH and increase of salt concentration lowered the absolute value of the zeta potential of the protein surface and led to a decrease of the equilibrium constant. The steric factor remained unchanged at about 31 at pH 5.5 and 6.0 and increased to 44.5 at pH 5.0 and 96.8 at pH 4.5, mainly as a result of the lower adsorption capacity of BSA at pH <5.5. Furthermore, the increase of the molecular volume of BSA at pH 4.5 would be an additional reason for the increase of the steric factor. Taking into account the effect of the pH and salt concentration on these parameters, the SMA model described the ion exchange equilibrium of protein more accurately.

Purification of proteins using displacement chromatography

Displacement chromatography has several advantages over the nonlinear elution technique, as well as the linear elution mode, such as the recovery of purified components at high concentrations, less tailing during elution, high throughput and high resolution. Displacer affinity and its utilization are the critical components of displacement chromatography. Particularly, the nonspecific interactions between the displacer and the stationary phase can be exploited to generate high affinity displacers. This chapter will discuss the design and execution of displacer selection and implementation in a separation specifically focusing on its utilization in ion exchange chromatography.

Investigation of the steric mass action formalism in the simulation of breakthrough curves on a monolithic and a packed bed column

The simulation of the behaviour of two proteins (cytochrom c and alpha-chymotrypsinogen) on two types of stationary phases (monolithic and porous particle-based) was attempted for non-linear (simulation of breakthrough curves) and linear (simulation of elution peaks) cation exchange chromatography. It was found that the combination of a stoichiometric model (steric mass action, SMA) with the lumped pore diffusion (POR) model allows a simulation of high predictive value. Using one set of SMA and transport parameters for a given column morphology and/or protein, breakthrough curves and peaks could be simulated that agreed well with the experimental data while no dependency on either the protein load or the mobile phase composition (salt content) was observed. One of the SMA parameters, namely the characteristic charge needed some slight adjustment (within the error of the experimental determination of this parameter) in order to optimise the fit.

Modeling ion-exchange adsorption of proteins in a spherical particle

This paper presents a simple model of single- and multicomponent protein adsorption in a spherical particle. The model includes radial diffusion of salt and protein in the liquid phase coupled to adsorption by an ion-exchange mechanism described by the steric mass action isotherm. The molecular diffusivities of the protein and salt are reduced in the model by a factor which accounts for the tortuous nature of the pores and pore constrictions. The model parameters are selected from published values in the chromatographic literature. Of particular interest are the observations of induced salt gradients during protein adsorption and of multicomponent displacement when more that one protein is adsorbed simultaneously. These results cannot be predicted on the basis of the traditional Langmuir isotherm or other currently available descriptions of adsorption. The use of such a model during stationary phase design is discussed.

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

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

Comparison of preparative characteristics of micro open parallel plate separators and microbore columns for concentration of trace species by displacement chromatography

The potential for preparative concentration of trace species by displacement chromatography in a micro open parallel plate separator (microOPPS) has been explored. A comparison of the performance of the microOPPS with micro open tubular columns (microOTC) has been presented. Using simulation models, the effects of operating and equilibrium parameters on throughput and yield have been determined. It is shown that the microOPPS can offer considerable advantages over the traditional microOTCs. Most significantly, throughputs can be enhanced by more than an order of magnitude in many cases. This is primarily due to the higher loading per cycle in the microOPPS, made possible by the ability to change the depth of the channel independent of the width. While yield is generally lower in the microOPPS, this effect can be overcome by the proper selection of operating conditions.

Mass influences in the performance of oligomeric poly(diallyldimethylammonium chloride) as displacer for cation-exchange displacement chromatography of proteins

A novel type of linear polyelectrolyte, namely poly-DADMAC [poly(diallyldimethylammonium chloride)], was prepared and studied as a displacer for cation-exchange displacement chromatography of proteins. In contrast to the commercially available polymers of that chemistry, the novel type of poly-DADMAC introduced here is characterized by a homogeneous linear structure, a narrow distribution of the (adjustable) molar mass as well as by a defined and homogeneous affinity for the stationary phase. Five poly-DADMACs of different size (17900 to 88000 g/mol) were prepared and compared with regard to their stationary phase affinity and protein separation potential, taking a mixture of basic proteins, namely lysozyme, cytochrome C, and ribonuclease A (from bovine pancreas), as an example. The steric mass action model was employed to aid method development. Under the chosen conditions (low ionic strength of the mobile phase guaranteeing strong binding of both the proteins and the displacer) the poly-DADMAC with the lowest molar masses proved to be the most efficient displacers for the basic proteins with a stationary phase affinity constant of 5.3 x 10(16) and a steric factor of 224. Using this substance as displacer, a sample mixture containing up to three proteins was separated and the proteins recovered at high yields (80-97%) and in high purity and concentration.

Optimization of ion-exchange displacement separations. II. Comparison of displacement separations on various ion-exchange resins

A variety of stationary-phase materials are currently available for the chromatographic purification of biomolecules. However, the effect of various resin characteristics on the performance of displacement chromatography has not been studied in depth. In Part I, a novel iterative scheme was presented for the rapid optimization of displacement separations in ion-exchange systems. In this article, the optimization scheme is employed to identify the optimum operating conditions for displacement separations on various ion-exchange resin materials. In addition, the effect of different classes of separation problems (e.g., diverging, converging or parallel affinity lines) on the performance of displacement separations is also presented. The solid film linear driving force model is employed in concert with the Steric Mass Action isotherm to describe the chromatographic behavior in these systems. The results presented in this article provide insight into the effects of resin capacity and efficiency as well as the type of separation problem on the performance of various ion-exchange displacement systems.

Comparison of particulate and continuous-bed columns for protein displacement chromatography

A conventional anion exchange column packed with porous particles (BioScale Q2), and a novel continuous-bed column (UNO Q1) were compared for displacement separation of dairy whey proteins with polyacrylic acid as displacer. The steric mass action model was investigated as a means to aid and accelerate this development. Characteristic charges and steric factors were measured for the proteins and the displacer according to the model, and used together with the affinity constant derived from the adsorption isotherms for simulations, as well as for the construction of the affinity and operating regime plots. If possible, the latter two were used to select conditions for the actual experiments. In the case of the particle-based column, experimental results and simulations did not agree. In addition, the operating regime plot could not be constructed. The affinity plot did predict the order in the displacement train correctly, but gave misleading information concerning the possible effect of a change in displacer concentration. This is taken to be a result of the porous nature of the particles, which handicaps, to some extent, the interaction of the proteins and the displacer molecules with the adsorptive surface. Results were considerably better in case of the continuous-bed column, where there is no intraparticulate surface.