Characterization and design of chemically selective cationic displacers using a robotic high‐throughput screen

A robotic high‐throughput displacer screen was developed and employed to identify chemically selective displacers for several protein pairs in cation exchange chromatography. This automated screen enabled the evaluation of a wide range of experimental conditions in a relatively short period of time. Displacers were evaluated at multiple concentrations for these protein pairs, and DC‐50 plots were constructed. Selectivity pathway plots were also constructed and different regimes were established for selective and exclusive separations. Importantly, selective displacement was found to be conserved for multiple protein pairs, demonstrating the technique to be applicable for a range of protein systems. Although chemically selective displacers were able to separate protein pairs that had similar retention in ion exchange but different surface hydrophobicities, they were not able to distinguish protein pairs with similar surface hydrophobicities. This corroborates that displacer‐protein hydrophobic interactions play an important role for this class of selective displacers. Important functional group moieties were established and efficient displacers were identified. These results demonstrate that the design of chemically selective displacers requires a delicate balance between the abilities to displace proteins from the resin and to bind to a selected protein. The use of robotic screening of displacers will enable the extension of chemically selective displacement chromatography beyond hydrophobic displacer‐protein interactions to other secondary interactions and more selective displacement systems. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Protected amino acids as novel low-molecular-weight displacers in cation-exchange displacement chromatography

Although the ability to carry out simultaneous concentration and purification in a single displacement step has significant advantages for downstream processing of pharmaceuticals, a major impediment to the implementation of displacement chromatography has been the lack of suitable displacer compounds. An important recent advance in the state of the art of displacement chromatography has been the discovery that low-molecular-weight dendritic polymers can be successfully employed as displacers for protein purification in ion-exchange systems. In this article, protected amino acid esters (based on arginine and lysine) are shown to be useful displacers for protein purification in cation-exchange systems. A dynamic affinity plot is employed to evaluate the affinity of these low-molecular-weight compounds under dis-placement conditions. In contrast to large polyelectroyte displacers, the efficacy of these low-molecular-weight displacers was shown to be dependent on both the initial carrier salt concentration and the displacer concentration. In addition to the funcamental interest generated by low-molecular-weight displacers, it is likely that these displacers will have significant operatioal advantages as compared with large polyelectrolyte displacers. (c) 1995 John Wiley & Sons, Inc.     

Mechanistic studies of displacer–protein binding in chemically selective displacement systems using NMR and MD simulations

A parallel batch screening technique was employed to identify chemically selective displacers which exhibited exclusive separation behavior for the protein pair α‐chymotrypsin/ribonuclease A on a strong cation exchange resin. Two selective displacers, 1‐(4‐chlorobenzyl)piperidin‐3‐aminesulfate and N′1′‐(4‐methyl‐quinolin‐2‐yl)‐ethane‐1,2‐diamine dinitrate, and one non‐selective displacer, spermidine, were selected as model systems to investigate the mechanism of chemically selective displacement chromatography. Saturation transfer difference (STD) NMR was used to directly evaluate displacer–protein binding. The results indicated that while binding occurred between the two chemically selective displacers and the more hydrophobic protein, α‐chymotrypsin, no binding was observed with ribonuclease A. Further, the non‐selective displacer, spermidine, was not observed to bind to either protein. Importantly, the binding event was observed to occur primarily on the aromatic portion of the selective displacers. Extensive molecular dynamic simulations of protein–displacer–water solution were also carried out. The MD results corroborated the NMR findings demonstrating that the binding of selective displacers occurred primarily on hydrophobic surface patches of α‐chymotrypsin, while no significant long term binding to ribonuclease A was observed. The non‐selective displacer did not show significant binding to either of the proteins. MD simulations also indicated that the charged amine group of the selective displacers in the bound state was primarily oriented towards the solvent, potentially facilitating their interaction with a resin surface. These results directly confirm that selective binding between a protein and displacer is the mechanism by which chemically selective displacement occurs. This opens up many possibilities for future molecular design of selective displacers for a range of applications. Biotechnol. Bioeng. 2009;102: 1428–1437. © 2008 Wiley Periodicals, Inc.     

Application of hydrophobic interaction displacement chromatography for an industrial protein purification

Recently it has been established that low molecular weight displacers can be successfully employed for the purification of proteins in hydrophobic interaction chromatography (HIC) systems. This work investigates the utility of this technique for the purification of an industrial protein mixture. The study involved the separation of a mixture of three protein forms, that differed in the C-terminus, from their aggregate impurities while maintaining the same relative ratio of the three protein forms as in the feed. A batch high-throughput screening (HTS) technique was employed in concert with fluorescence spectroscopy for displacer screening in these HIC systems. This methodology was demonstrated to be an effective tool for identifying lead displacer candidates for a particular protein/stationary-phase system. In addition, these results indicate that surfactants can be employed at concentrations above their CMCs as effective displacers. Displacement of the recombinant proteins with PEG-3400 and the surfactant Big Chap was shown to increase the productivity as compared to the existing step-gradient elution process.     

Cation-exchange displacement chromatography of proteins with protamine displacers: effect of induced salt gradients.

Protamine was investigated for its utility as a protein displacer in cation-exchange systems. Although the protamine solution contained several variants of the molecule, the high affinity of all of the components in this heterogeneous biopolymer enabled it to act as an efficient protein displacer. To facilitate parameter estimation of the protamine, a preliminary purification was carried out by preparative elution chromatography. Chromatographic parameters of both the feed proteins and protamine displacer were obtained for use in a multicomponent steric mass action ion-exchange displacement model. Model simulations were compared to displacement results under both moderate and intense induced salt gradient conditions. In both cases, excellent agreement was obtained between the displacement experiments and theoretical predictions. In addition, these studies serve to dramatize the importance of induced salt gradients in ion-exchange displacement systems.     

Comparison of linear gradient and displacement separations in ion-exchange systems

The linear gradient mode of chromatography is the most widely employed mode of operation in ion-exchange chromatographic separations. However, in recent years, the displacement mode has received considerable attention because of its promise of high throughput and high resolution. To enable a comparison of these two modes of chromatography, it is essential to identify the optimum operating conditions for each. We employed an iterative algorithm to carry out the necessary optimization. The Steric Mass Action model of ion-exchange chromatography is used in concert with the solid-film linear-driving force model to describe the chromatographic behavior of the solutes in these systems. The performances of displacement and gradient modes of chromatography are compared for different types of separation problems. It turns out that for "easy" separations, both the modes are equally effective. However, for challenging separations, the displacement mode is superior to the gradient mode. Our results shed significant light on the performance of gradient and displacement modes in protein ion-exchange systems.     

SCX separation of recombinant thrombolytic protein from complex biological feeds

The purification of recombinant thrombolytic protein from a crude fermentation broth mixture was examined in strong cation exchange (SCX) Chromatographic system. SCX system was shown to exhibit unique selectivity for the recombinant protein broth mixture. While SCX system showed lower total binding capacity for the recombinant protein than Anti-body Exchange system, it showed sharper separation boundaries in both displacement and step gradient module. The research with the SCX indicated that this separating system could be successfully employed in the displacement mode using DEAE-dextran as the displacer.     

Purification of oligonucleotides by high affinity, low molecular weight displacers

High affinity, low molecular weight anionic displacers were successfully employed for the purification of antisense oligonucleotides. Several important structural characteristics were identified that contribute to the affinity of low molecular weight displacers to a hydrophilized polystyrene divinyl benzene anion exchanger. Sulfonic acid groups were found to possess higher affinity than carboxylic acid and phosphate functionalities, and nonspecific interactions (particularly hydrophobic interactions) were shown to play a major role in the retention process on this stationary phase material. Using this information, two high affinity, low molecular weight displacers were identified. These molecules are relatively inexpensive organic dyes that possess multiple sulfonic acid moieties, as well as aromatic functionalities, which increase nonspecific interactions with the stationary phase. These high affinity displacers, which can be readily detected, were then employed to displace several strongly retained antisense oligonucleotides that could not be displaced by previously established low molecular weight displacers. The displacement process resulted in very high purities of the antisense oligonucleotides. The results presented in this paper are significant in that they demonstrate that low molecular weight displacers for ion-exchange chromatography can possess equal to or greater affinities than their higher molecular weight counterparts, when nonspecific interactions with the stationary phase are exploited. In addition, the results illustrate the high resolutions possible with displacement chromatography and demonstrate an attractive technology for the process scale purification of oligonucleotides.     

Purification process development of a recombinant monoclonal antibody expressed in glycoengineered Pichia pastoris

A robust and scalable purification process was developed to quickly generate antibody of high purity and sufficient quantity from glycoengineered Pichia pastoris fermentation. Protein A affinity chromatography was used to capture the antibody from fermentation supernatant. A pH gradient elution was applied to the Protein A column to prevent antibody precipitation at low pH. Antibody from Protein A chromatography contained some product related impurities, which were the misassembling of cleaved heavy chain, heavy chain and light chain. It also had some process related impurities, including Protein A residues, endotoxin, host cell DNA and proteins. Cation exchange chromatography with optimal NaCl gradient at pH 4.5-6.0 efficiently removed these product and process related impurities. The antibody from glycoengineered P. pastoris was comparable to its commercial counterpart in heterotetramer folding, physical stability and binding affinity.     

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.     

Hydrophobic displacement chromatography of proteins

Displacement chromatography of proteins was successfully carried out in both hydrophobic interaction and reversed-phase chromatographic systems using low-molecular weight displacers. The displacers employed for hydrophobic displacement chromatography were water soluble, charged molecules containing several short alkyl and/or aryl groups. Spectroscopy was employed to verify the absence of structural changes to the proteins displaced on these hydrophobic supports. Displacement chromatography on a reversed-phase material was employed to purify a growth factor protein from its closely related variants, demonstrating the high resolutions that can be achieved by hydrophobic displacement chromatography. This process combines the high-resolution/high-throughput characteristics of displacement chromatography with the unique selectivity of these hydrophobic supports and offers the chromatographic engineer a powerful tool for the preparative purification of proteins.     

A two step displacement and affinity chromatography purification in lactate dehydrogenase recovery from beef heart extract

Lactate dehydrogenase from beef heart extract was purified by displacement chromatography on a Tris Acryl DEAE. Chondroitin sulphate C, alginate and Eudragits were tried as displacers. Displacement, in conjunction with a subsequent affinity step, gave high purifications and yields. The potential of this operational mode as an early step in protein recovery and the use of L and S forms of Eudragit as cheap readily available and non-toxic displacers has been demonstrated in this work.     

Displacement to separate host‐cell proteins and aggregates in cation‐exchange chromatography of monoclonal antibodies

An efficient and consistent method of monoclonal antibody (mAb) purification can improve process productivity and product consistency. Although protein A chromatography removes most host‐cell proteins (HCPs), mAb aggregates and the remaining HCPs are challenging to remove in a typical bind‐and‐elute cation‐exchange chromatography (CEX) polishing step. A variant of the bind‐and‐elute mode is the displacement mode, which allows strongly binding impurities to be preferentially retained and significantly improves resin utilization. Improved resin utilization renders displacement chromatography particularly suitable in continuous chromatography operations. In this study we demonstrate and exploit sample displacement between a mAb and impurities present at low prevalence (0.002%–1.4%) using different multicolumn designs and recycling. Aggregate displacement depends on the residence time, sample concentration, and solution environment, the latter by enhancing the differences between the binding affinities of the product and the impurities. Displacement among the mAb and low‐prevalence HCPs resulted in an effectively bimodal‐like distribution of HCPs along the length of a multi‐column system, with the mAb separating the relatively more basic group of HCPs from those that are more acidic. Our findings demonstrate that displacement of low‐prevalence impurities along multiple CEX columns allows for selective separation of mAb aggregates and HCPs that persist through protein A chromatography.     

Branch capture reactions: displacers derived from asymmetric PCR.

Branch capture reactions (BCR) contain three DNA species: (i) a recipient restriction fragment terminating in an overhang, (ii) a displacer strand containing two adjacent sequences, with one complementary to the overhang and to contiguous nucleotides within the recipient duplex and (iii) a linker which is complementary to the second displacer sequence. Branched complexes containing all three species may be captured by ligation of the linker to the recipient overhang. The use of 5-MedC in the displacer facilitates BCR. High temperature ligation with a thermostable enzyme increased specificity for ligation to the correct recipient in a complex mixture of restriction fragments. Displacer synthesis by PCR permitted separate reactions of formation of stable displacement complexes and of high-temperature ligation. Ethylene glycol-containing buffer permitted PCR with 5-MedCTP or high G + C products using thermostable polymerases. BCR may be used to modify the ends of one recipient DNA duplex in a population of duplex DNA fragments. Modification of the recipient could be used to facilitate detection, affinity chromatography or cloning. By using PCR to obtain a BCR displacer, the sequence non-homologous to the recipient duplex may be expanded to include the sequence of a selectable marker, thus facilitating chromosome walking.     

Modeling of non-ideal displacement separation in immobilized metal ion affinity chromatography

To predict complex behavior in protein displacement systems of immobilized metal ion affinity chromatography (IMAC), numerical simulation of non-linear chromatography was developed and compared with the ideal solution of the model. The theoretical and experimental results demonstrate that the IMAC model can be successfully employed in predicting induced mobile phase modifier gradients and complex behavior in metal affinity displacement chromatography. The solute movement analysis is able to predict the displacement separation well characterized by the intersections of the operation line under the induced mobile phase modifier and effective displacer concentrations.     

Purification of recombinant brain derived neurotrophic factor using reversed phase displacement chromatography

This work investigates the utility of RPLC displacement chromatography for the purification of recombinant brain derived neurotrophic factor (rHu-BDNF) from its variants and E. coli. protein (ECP) impurities. The closely associated variants (six in total) differ by one amino acid from the native BDNF and thus pose a challenging separation problem. Several operational parameters were investigated to study their effects on the yield of the displacement process. The results indicated that the concentration of trifluoroacetic acid (TFA) in the buffer was a key factor in achieving the desired purification. Displacement chromatography on an analytical scale column resulted in extremely high purity and yield in a single chromatographic step. The process was successfully scaled-up with respect to particle and column diameter. The production rate of a pilot scale RPLC displacement process was shown to be 23 times higher than the combined production rates of the current preparative ion exchange and hydrophobic interaction gradient elution steps that are used to remove variant and ECP impurities, respectively.     

Operating parameters for glutamic acid crystallization in displacement ion exchange chromatography

Glutamic acid can be crystallized inside cation exchange column when displacer NaOH concentration is high enough to concentrate displaced glutamic acid beyond its solubility limit. Resulting crystal layer of glutamic acid was moved with liquid phase through the column, and thus could be eluted from the column and recovered in fraction collector. For the purpose of enhancing crystal recovery, effects of operating parameters on the crystal formation were investigated. The increase in the degree of crosslinking of resin favored crystal recovery because of its low degree of swelling. Higher concentration of displacer NaOH was advantageous. If NaOH concentration is too high, however, crystal recovery was lowered due to the solubility-enhancing effects of high pH and ionic strength. The decrease of mobile phase flow rate enhanced crystal recovery because enough time to attain local equilibrium could be provided, but film diffusion would control the overall crystal formation with extremely low flow rate. Lower temperature reduced solubility of glutamic acid and thus favored crystal formation unless the rate of ion exchange was severely reduced. The ion exchange operated by displacement mode coupled with crystallization was advantageous in reducing the burden of further purification steps and in preventing purity-loss resulted from overlapping between adjacent bands.     

Affinity chromatography with amniotic fluid somatomedin binding protein in the purification of insulin-like growth factor I

A simplified procedure has been developed for the isolation of insulin-like growth factor I from human plasma by use of affinity chromatography with the somatomedin binding protein. After acidification of human plasma and separation of insulin-like growth factor I and endogenous binding protein by cation exchange chromatography on SP-Sephadex the material was passed through a column packed with pure human amniotic fluid binding protein covalently coupled to Sepharose. The bound insulin-like growth factors I and II were eluted by 1M acetic acid and separated on a Mono S cation exchange column by use of a salt gradient. The 30 micrograms insulin-like growth factor I and 18 micrograms insulin-like growth factor II recovered from 1 liter plasma gave an overall recovery of 30% for insulin-like growth factor I but only 2.5% for insulin-like growth factor II.     

Vacancy affinity capillary electrophoresis to study competitive protein–drug binding

The suitability of the vacancy affinity capillary electrophoretic method (VACE) for study of displacement of a target drug from a protein by simultaneously administered drugs was investigated. As test system, the displacement of warfarin from bovine serum albumin (BSA) by furosemide and phenylbutazone was selected. It appears that the displacement can be observed well from the shift of the actual mobility of warfarin when a displacer drug is added. Also, the competitive action of the displacer drugs (affinity for BSA) is clearly visible. The VACE method seems to be attractive for rapid assesssment of information about the competitive properties of coadministered compounds.