Interaction mechanism of mono-PEGylated proteins in electrostatic interaction chromatography

The retention and binding mechanisms in electrostatic interaction-based chromatography (ion-exchange chromatography) of PEGylated proteins (covalent attachment of polyethylene glycol chains to protein) were investigated using our previously developed model. Lysozyme and bovine serum albumin were chosen as model proteins. The retention volume of PEGylated proteins shifted to lower elution volumes with increasing PEG molecular weight compared with the non-modified (native) protein retention volume. However, PEGylation did not affect the number of binding sites appreciably. The enzyme activity of PEGylated lysozyme measured with a standard insoluble substrate in suspension decreased considerably, whereas the activity with a soluble small-molecule substrate did not drop significantly. These findings indicate that when a protein is mono-PEG-ylated, the binding site is not affected and the elution volume reduces due to the steric hindrance between PEGylated protein and ion-exchange ligand.     

Effects of protein conformational changes on separation performance in electrostatic interaction chromatography: unfolded proteins and PEGylated proteins

As it is important to understand how protein conformational changes affect the separation performance in ion exchange chromatography (IEC), we investigated two model systems, unfolded proteins (lysozyme and bovine serum albumin) with urea and dithiothreitol, and PEGylated proteins (lysozyme attached with polyethyleneglycol molecular weight 5000). Linear gradient elution IEC experiments were carried out and the data were analysed by our model previously presented in order to obtain the binding site value B and the peak salt concentration I(R). Unfolded proteins (bovine serum albumin and lysozyme) with urea and dithiothreitol showed weaker retention and larger binding site values compared with the values for native proteins. Multiple PEGylated lysozyme peaks were separated, and eluted earlier than the native peak appeared. There is a good correlation between B and I(R) for PEGylated lysozymes.     

Structure‐Based Site‐Specific PEGylation of Fibroblast Growth Factor 2 Facilitates Rational Selection of Conjugate Sites

Polyethylene glycol modification (PEGylation) can enhance the pharmacokinetic properties of therapeutic proteins by the attachment of polyethylene glycol (PEG) to the surface of a protein to shield the protein surface from proteolytic degradation and limit aggregation. However, current PEGylation strategies often reduce biological activity, potentially as a result of steric hindrance of PEG. Overall, there are no structure‐based guidelines for selection of conjugate sites that retain optimal biological activity with improved pharmacokinetic properties. In this study, site‐specific PEGylation based on the FGF2‐FGFR1‐heparin complex structure is performed. The effects of the conjugate sites on protein function are investigated by measuring the receptor/heparin binding affinities of the modified proteins and performing assays to measure cell‐based bio‐activity and in vivo stability. Comprehensive analysis of these data demonstrates that PEGylation of FGF2 that avoids the binding sites for fibroblast growth factor receptor 1 (FGFR1) and heparin provides optimal pharmacokinetic enhancement with minimal losses to biological activity. Animal experiments demonstrate that PEGylated FGF2 exhibits greater efficacy in protecting against traumatic brain injury‐induced brain damage and neurological functions than the non‐modified FGF2. This rational structure‐based PEGylation strategy for protein modification is expected to have a major impact in the area of protein‐based therapeutics.     

PEG chain length impacts yield of solid-phase protein PEGylation and efficiency of PEGylated protein separation by ion-exchange chromatography: Insights of mechanistic models

The mechanisms behind protein PEGylation are complex and dictated by the structure of the protein reactant. Hence, it is difficult to design a reaction process which can produce the desired PEGylated form at high yield. Likewise, efficient purification processes following protein PEGylation must be constructed on an ad hoc basis for each product. The retention and binding mechanisms driving electrostatic interaction-based chromatography (ion-exchange chromatography) of PEGylated proteins (randomly PEGylated lysozyme and mono-PEGylated bovine serum albumin) were investigated, based on our previously developed model Chem. Eng. Technol. 2005, 28, 1387–1393. PEGylation of each protein resulted in a shift to a smaller elution volume compared to the unmodified molecule, but did not affect the number of binding sites appreciably. The shift of the retention volume of PEGylated proteins correlated with the calculated thickness of PEG layer around the protein molecule. Random PEGylation was carried out on a column (solid-phase PEGylation) and the PEGylated proteins were separated on the same column. Solid-phase PEGylation inhibited the production of multi-PEGylated forms and resulted in a relatively low yield of selective mono-PEGylated form. Pore diffusion may play an important role in solid-phase PEGylation. These results suggest the possibility of a reaction and purification process development based on the mechanistic model for PEGylated proteins on ion exchange chromatography.     

Applicability of Chromatographic Co‐Elution for Antibiotic Target Identification

Identification of the molecular target is a crucial step in evaluating novel antibiotics. To support target identification, a label‐free method based on chromatographic co‐elution has previously been developed. Target identification by chromatographic coelution (TICC) exploits the alteration of the elution profile of target‐bound drug versus free drug in ion exchange (IEX) chromatography to identify potential target proteins from elution fractions. The applicability of TICC for antibiotic research is investigated by evaluating which proteins, that is, putative targets, can be monitored in Bacillus subtilis. Coelution of components of known protein complexes provides a read‐out for how well the native state of proteins is conserved during chromatography. Rifampicin, which targets RNA polymerase, is used in a proof‐of‐concept study.     

A liquid chromatographic method for determination of the modification degree of proteins: PEGylated arginase as an example

A liquid chromatographic method was developed to determine the modification degree of PEGylated proteins. This method effectively separated free polyethylene glycol (PEG) from other species in conjugation mixtures on a C4 reversed-phase column using water-acetonitrile gradient elution. Then the concentrations of free PEG were determined according to the integrated area under the curve of its evaporative light scattering detector (ELSD) signal, which was normalized by the PEG standard with similar molecular weights. The actual numbers of PEG attached to proteins, not those of lysines modified, were calculated. This method was performed with PEGylated arginase mixtures as an example and showed clear advantages over 2,4,6-trinitrobenzenesulfonic acid (TNBS) assays.     

Improving enantiomeric resolutions by avoiding peak distortion effects in on‐line coupled liquid chromatography to gas chromatography

In this work, we study the effect of different variables affecting elution profile distortion on the enantiomeric resolution eventually achievable when working with on‐line coupled liquid chromatography to gas chromatography (LC‐GC). Specifically, the proposed configuration combines achiral reversed‐phase liquid chromatography (RPLC) and chiral gas chromatography (enantio‐GC), with heptakis‐(2,3,6‐tri‐O‐methyl)‐β‐cyclodextrin as enantioselective stationary phase to analyse target fractions transferred (from LC to GC) via the through oven transfer adsorption desorption (TOTAD) interface. The high degree of orthogonality resulting from the combination of two chromatographic columns having very different separation mechanisms (and also requiring mobile phases in distinct physical states), as well as integration of the sample preparation step in the first dimension of the system, significantly contributed to exploit the performance of the proposed two‐dimensional approach. Occasional adverse effects, which may result in severe peak distortions during LC‐GC analysis and could be explained by flow instabilities due to viscous fingering, are circumvented by using the outstanding capacity of the TOTAD interface for achieving effective elimination of the eluent arriving from the LC preseparation.     

Competitive adsorption of labeled and native protein in confocal laser scanning microscopy

Confocal laser scanning microscopy has been previously applied to the study of protein uptake in porous chromatography resins. This method requires labeling the protein with a fluorescent probe. The labeled protein is then diluted with a large quantity of native protein so that the fluorescence intensity is a linear function of the labeled protein concentration. Ideally, the attachment of a fluorescent probe should not affect the affinity of the protein for the stationary phase; however, recent experimental work has shown that this assumption is difficult to satisfy. In the present study, we present a mathematical model of protein diffusion and adsorption in a single adsorbent particle. The differences in adsorption behavior of labeled and native protein are accounted for by treating the system as a two-component system (labeled and native protein) described by the steric mass action isotherm (SMA). SMA parameters are regressed from experimental linear gradient elution data for lysozyme and lysozyme-dye conjugates (for the fluorescent dyes Cy3, Cy5, Bodipy FL, and Atto635). When the regressed parameters are employed in the model, an overshoot in the labeled lysozyme concentration is predicted for Cy5- and Bodipy-labeled lysozyme, but not for Atto635-labeled lysozyme. The model predictions agree qualitatively well with recent work showing the dependence of the concentration overshoot on the identity of the attached dye and provide further evidence that the overshoot is likely caused by the change of binding characteristics due to the fluorescent label.     

Clarification and capture of high‐concentration refold pools for E. coli‐based therapeutics using expanded bed adsorption chromatography

Expanded bed adsorption (EBA) chromatography was investigated for clarification and capture of high‐concentration refold pools of Escherichia coli‐based therapeutics. Refolding of denatured inclusion bodies (IBs) at high protein concentration significantly improved product throughput; however, direct filtration of the refold materials became very challenging because of high content of protein precipitates formed during refolding. In addition, irreversible protein precipitation caused by high local concentration was encountered in packed bed capture during cation exchange chromatography elution, which limited column loading capacity and capture step productivity. In this study, the two issues are addressed in one unit operation by using EBA. Specifically, EBA can handle feed streams with significant amount of particles and precipitates, which eliminated the need for refold pool clarification through filtration. The relatively broad EBA elution profile is particularly suitable for proteins of low solubility and can effectively avoid product loss previously associated with on‐column precipitation during capture. As the EBA resin (RHOBUST^® FastLine SP IEX) used here has unique properties, it can be operated at high linear velocity (800–1,600 cm/h), while achieving a selectivity and impurity clearance largely comparable to the packed bed resin of the same ligand chemistry (SP Sepharose FF). Furthermore, the filtration of the EBA elution pool is easily manageable within facility capability. Overall, this study demonstrates that the EBA process helps debottleneck the purification of high‐turbidity refold pools by removing precipitates and concurrently capturing the product, which can be applied to other E. coli‐based therapeutics that also requires refolding of IBs. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 30:113–123, 2014     

High-throughput screening of chromatographic separations: IV. Ion-exchange

Ion-exchange (IEX) chromatography steps are widely applied in protein purification processes because of their high capacity, selectivity, robust operation, and well-understood principles. Optimization of IEX steps typically involves resin screening and selection of the pH and counterion concentrations of the load, wash, and elution steps. Time and material constraints associated with operating laboratory columns often preclude evaluating more than 20-50 conditions during early stages of process development. To overcome this limitation, a high-throughput screening (HTS) system employing a robotic liquid handling system and 96-well filterplates was used to evaluate various operating conditions for IEX steps for monoclonal antibody (mAb) purification. A screening study for an adsorptive cation-exchange step evaluated eight different resins. Sodium chloride concentrations defining the operating boundaries of product binding and elution were established at four different pH levels for each resin. Adsorption isotherms were measured for 24 different pH and salt combinations for a single resin. An anion-exchange flowthrough step was then examined, generating data on mAb adsorption for 48 different combinations of pH and counterion concentration for three different resins. The mAb partition coefficients were calculated and used to estimate the characteristic charge of the resin-protein interaction. Host cell protein and residual Protein A impurity levels were also measured, providing information on selectivity within this operating window. The HTS system shows promise for accelerating process development of IEX steps, enabling rapid acquisition of large datasets addressing the performance of the chromatography step under many different operating conditions.     

Optimization of step gradient separations: Consideration of nonlinear adsorption

Nonlinear adsorption plays an important role in determining the chromatographic behavior of proteins in preparative ion-exchange chromatography. In this article, the steric mass action (SMA) isotherm is used in conjunction with a mass transport model to describe nonlinear cation-exchange chromatography. Excellent agreement is observed between simulated and experimental step gradient separations of the proteins alpha-chymotryp-sinogen A, cytochrome C, and lysozyme. A systematic method of selecting the optimum step gradient program for a given separation problem is presented and employed to study optimization of step gradient chromatography under conditions of high mass loading. This article includes consideration of the effects of the adsorption properties of the feed stream, the feed stream concentration, protein solubility, and otherconstraints on the optimum separation conditions.(c) John Wiley & Sons, Inc.     

Molecular Insight into the Steric Shielding Effect of PEG on the Conjugated Staphylokinase: Biochemical Characterization and Molecular Dynamics Simulation

PEGylation is a successful approach to improve potency of a therapeutic protein. The improved therapeutic potency is mainly due to the steric shielding effect of PEG. However, the underlying mechanism of this effect on the protein is not well understood, especially on the protein interaction with its high molecular weight substrate or receptor. Here, experimental study and molecular dynamics simulation were used to provide molecular insight into the interaction between the PEGylated protein and its receptor. Staphylokinase (Sak), a therapeutic protein for coronary thrombolysis, was used as a model protein. Four PEGylated Saks were prepared by site-specific conjugation of 5 kDa/20 kDa PEG to N-terminus and C-terminus of Sak, respectively. Experimental study suggests that the native conformation of Sak is essentially not altered by PEGylation. In contrast, the bioactivity, the hydrodynamic volume and the molecular symmetric shape of the PEGylated Sak are altered and dependent on the PEG chain length and the PEGylation site. Molecular modeling of the PEGylated Saks suggests that the PEG chain remains highly flexible and can form a distinctive hydrated layer, thereby resulting in the steric shielding effect of PEG. Docking analyses indicate that the binding affinity of Sak to its receptor is dependent on the PEG chain length and the PEGylation site. Computational simulation results explain experimental data well. Our present study clarifies molecular details of PEG chain on protein surface and may be essential to the rational design, fabrication and clinical application of PEGylated proteins.     

Multi‐dimensional fractionation and characterization of crude protein mixtures: Toward establishment of a database of protein purification process development parameters

A multi‐dimensional fractionation and characterization scheme was developed for fast acquisition of the relevant molecular properties for protein separation from crude biological feedstocks by ion‐exchange chromatography (IEX), hydrophobic interaction chromatography (HIC), and size‐exclusion chromatography. In this approach, the linear IEX isotherm parameters were estimated from multiple linear salt‐gradient IEX data, while the nonlinear IEX parameters as well as the HIC isotherm parameters were obtained by the inverse method under column overloading conditions. Collected chromatographic fractions were analyzed by gel electrophoresis for estimation of molecular mass, followed by mass spectrometry for protein identification. The usefulness of the generated molecular properties data for rational decision‐making during downstream process development was equally demonstrated. Monoclonal antibody purification from crude hybridoma cell culture supernatant was used as case study. The obtained chromatographic parameters only apply to the employed stationary phases and operating conditions, hence prior high throughput screening of different chromatographic resins and mobile phase conditions is still a prerequisite. Nevertheless, it provides a quick, knowledge‐based approach for rationally synthesizing purification cascades prior to more detailed process optimization and evaluation. Biotechnol. Bioeng. 2012; 109: 3070–3083. © 2012 Wiley Periodicals, Inc.     

Zonal rate model for stacked membrane chromatography part II: characterizing ion-exchange membrane chromatography under protein retention conditions

The Zonal Rate Model (ZRM) has previously been shown to accurately account for contributions to elution band broadening, including external flow nonidealities and radial concentration gradients, in ion-exchange membrane (IEXM) chromatography systems operated under nonbinding conditions. Here, we extend the ZRM to analyze and model the behavior of retained proteins by introducing terms for intra-column mass transfer resistances and intrinsic binding kinetics. Breakthrough curve (BTC) data from a scaled-down anion-exchange membrane chromatography module using ovalbumin as a model protein were collected at flow rates ranging from 1.5 to 20 mL min(-1). Through its careful accounting of transport nonidealities within and external to the membrane stack, the ZRM is shown to provide a useful framework for characterizing putative protein binding mechanisms and models, for predicting BTCs and complex elution behavior, including the common observation that the dynamic binding capacity can increase with linear velocity in IEXM systems, and for simulating and scaling separations using IEXM chromatography. Global fitting of model parameters is used to evaluate the performance of the Langmuir, bi-Langmuir, steric mass action (SMA), and spreading-type protein binding models in either correlating or fundamentally describing BTC data. When combined with the ZRM, the bi-Langmuir, and SMA models match the chromatography data, but require physically unrealistic regressed model parameters to do so. In contrast, for this system a spreading-type model is shown to accurately predict column performance while also providing a realistic fundamental explanation for observed trends, including an observed increase in dynamic binding capacity with flow rate.     

The membrane skeleton of erythrocytes: models of its effect on lateral diffusion

The membrane skeleton, a network of structural proteins attached to the cytoplasmic surface of the plasma membrane, hinders lateral diffusion of integral proteins. 2. In some types of cells, such as epithelial cells and nerve cells, the obstruction of lateral diffusion by the membrane skeleton is one of the mechanisms by which proteins are localized to domains on the cell surface. 3. The effect of the membrane skeleton on lateral diffusion may involve steric hindrance, transient binding or both. Three pictures of the effect are reviewed, the discrete barrier model, the continuous barrier model and the transient binding model. 4. Experiments to distinguish the models are discussed.     

Fast and automated functional classification with MED‐SuMo: An application on purine‐binding proteins

Ligand–protein interactions are essential for biological processes, and precise characterization of protein binding sites is crucial to understand protein functions. MED‐SuMo is a powerful technology to localize similar local regions on protein surfaces. Its heuristic is based on a 3D representation of macromolecules using specific surface chemical features associating chemical characteristics with geometrical properties. MED‐SMA is an automated and fast method to classify binding sites. It is based on MED‐SuMo technology, which builds a similarity graph, and it uses the Markov Clustering algorithm. Purine binding sites are well studied as drug targets. Here, purine binding sites of the Protein DataBank (PDB) are classified. Proteins potentially inhibited or activated through the same mechanism are gathered. Results are analyzed according to PROSITE annotations and to carefully refined functional annotations extracted from the PDB. As expected, binding sites associated with related mechanisms are gathered, for example, the Small GTPases. Nevertheless, protein kinases from different Kinome families are also found together, for example, Aurora‐A and CDK2 proteins which are inhibited by the same drugs. Representative examples of different clusters are presented. The effectiveness of the MED‐SMA approach is demonstrated as it gathers binding sites of proteins with similar structure‐activity relationships. Moreover, an efficient new protocol associates structures absent of cocrystallized ligands to the purine clusters enabling those structures to be associated with a specific binding mechanism. Applications of this classification by binding mode similarity include target‐based drug design and prediction of cross‐reactivity and therefore potential toxic side effects.     

Site-specific PEGylation of bone morphogenetic protein-2 cysteine analogues

Three cysteine analogues of bone morphogenetic protein (BMP)-2, BMP2A2C, BMP2N56C, and BMP2E96C, were generated in order to enable the attachment of SH-reactive poly(ethylene glycol) (PEG) at specific sites. Three different approaches (Ap) were used for SH-specific PEGylation: (Ap1) reaction of glutathione activated proteins with thiol PEG; (Ap2) reaction of DTT reduced proteins with orthopyridyl disulfide PEG; (Ap3) reaction of DTT reduced proteins with maleimide PEG. Non-, mono-, and di-PEGylated BMP-2 analogues could be separated by RP-HPLC. Trypsin digestion of PEGylated proteins and Trypsin and GluC double-digestion of N-ethylmaleimide-labeled proteins confirmed that the modifications were site-specific. Surface plasmon resonance analysis of type I and type II receptor binding of the PEGylated BMP-2 analogues revealed that all three PEGylation approaches were equivalent. PEGylation at positions 2 and 96 caused a similar decrease in receptor affinity. PEGylation at position 56 resulted in a larger decrease in affinity for both types of receptors. Mono-PEGylated BMP-2 analogues exhibited intermediate affinities in comparison with unmodified and di-PEGylated proteins. However, the biological activity of the PEGylated BMP-2 analogues as measured in alkaline phosphatase assay was higher than BMP-2 wild-type for the PEGylated BMP2A2C, slightly reduced for the BMP2N56C, and strongly reduced for the BMP2E96C. These results taken together indicate that specific attachment of PEG at engineered sites of BMP-2 is possible and that the attachment site is critical for biological activity. Furthermore, the biological activity of PEGylated BMP-2 analogues in cell culture seems to be determined not only by receptor affinity, but also by other factors such as protein solubility and stability. It is also discussed that the attached PEG interferes with the binding of BMP-2 to modulator proteins, co-receptors, or heparinic sites of proteoglycans in the extracellular matrix.     

Development of a polishing step using a hydrophobic interaction membrane adsorber with a PER.C6®‐derived recombinant antibody

Membrane chromatography has already proven to be a powerful alternative to polishing columns in flow‐through mode for contaminant removal. As flow‐through utilization has expanded, membrane chromatography applications have included the capturing of large molecules, including proteins such as IgGs. Such bind‐and‐elute applications imply the demand for high binding capacity and larger membrane surface areas as compared to flow‐through applications. Given these considerations, a new Sartobind Phenyl? membrane adsorber was developed for large‐scale purification of biomolecules based on hydrophobic interaction chromatography (HIC) principles. The new hydrophobic membrane adsorber combines the advantages of membrane chromatography—virtually no diffusion limitation and shorter processing time—with high binding capacity for proteins comparable to that of conventional HIC resins as well as excellent resolution. Results from these studies confirmed the capability of HIC membrane adsorber to purify therapeutic proteins with high dynamic binding capacities in the range of 20 mg‐MAb/cm³‐membrane and excellent impurity reduction. In addition the HIC phenyl membrane adsorber can operate at five‐ to ten‐fold lower residence time when compared to column chromatography. A bind/elute purification step using the HIC membrane adsorber was developed for a recombinant monoclonal antibody produced using the PER.C6® cell line. Loading and elution conditions were optimized using statistical design of experiments. Scale‐up is further discussed, and the performance of the membrane adsorber is compared to a traditional HIC resin used in column chromatography. Biotechnol. Bioeng. 2010; 105: 296–305. © 2009 Wiley Periodicals, Inc.     

Protein carboxyl amidation increases the potential extent of protein polyethylene glycol conjugation

Chemical coupling of polyethylene glycol (PEG) to therapeutic proteins reduces their immunogenicity and prolongs their circulating half-life. The limitation of this approach is the number and distribution of sites on proteins available for PEGylation (the N terminus and the -amino group of lysines). To increase the extent of PEGylation, we have developed a method to increase the number of PEGylation sites in a model protein, recombinant methionine alpha,gamma-lyase (recombinant methioninase; rMETase), an enzyme cancer therapeutic cloned from Pseudomonas putida. rMETase was first PEGylated with methoxypolyethylene glycol succinimidyl glutarate-5000 with a molar ratio of PEG:rMETase of 15:1. The carboxyl groups of the initially PEGylated protein were then conjugated with diaminobutane, resulting in carboxyl amidation. This reaction was catalyzed by 1-ethyl-3-(3-dimethylaminopropyl) carbodiimide, a water-soluble carbodiimide. The steric hindrance provided by the PEG chains already coupled to the protein prevented cross-linking between rMETase molecules during the carboxyl amidation reaction. The carboxyl-amidated PEGylated rMETase was hyper-PEGylated at a molar ratio of PEG to PEG-rMETase of 60:1. Biochemical analysis indicated that 13 PEG chains were coupled to each subunit of rMETase after hyper-PEGylation compared with 6-8 PEG chains attached to the non-carboxyl-amidated PEG-rMETase. Approximately 15-20% of the non-PEGylated rMETase activity was retained in the hyper-PEGylated molecule. Immunogenicity of the hyper-PEG-rMETase was significantly reduced relative to PEG-rMETase and rMETase. Initial results suggest that hyper-PEGylation may become a new strategy for PEGylation of protein biologics.     

Preparation, characterization and in vitro bioactivity of N-terminally PEGylated staphylokinase dimers

PEGylation can improve the therapeutic efficacy of proteins by increasing serum half-life of proteins and reducing immunogenicity and antigenicity. However, PEGylation results in a substantial loss of the bioactivity of proteins due to the steric hindrance of polyethylene glycol (PEG). Dimerization of the proteins is an efficient approach to increase the bioactivity of the PEG-protein conjugates. Here, staphylokinase (SAK) was used due to its therapeutic potential for coronary thrombolysis. SAK dimers (dSAK) were prepared by engineering cysteine residue at the C-terminus of SAK and dimerization of the cysteine residue with 1,4-bismaleimidobutane. PEG aldehyde was used for site-specific PEGylation of dSAK at one of its two N-termini. Structural analysis indicated that dimerization of SAK can decrease the steric hindrance of PEG and increase the binding affinity of PEG-SAK to plasminogen. Dimerization of SAK increased the relative bioactivity of PEG-SAK from 39.0% to 62.0%. Therefore, site-specifically PEGylated dSAK at one of its two N-termini has higher bioactivity than the N-terminal PEGylated SAK.