Weak partitioning chromatography for anion exchange purification of monoclonal antibodies

Weak partitioning chromatography (WPC) is an isocratic chromatographic protein separation method performed under mobile phase conditions where a significant amount of the product protein binds to the resin, well in excess of typical flowthrough operations. The more stringent load and wash conditions lead to improved removal of more tightly binding impurities, although at the cost of a reduction in step yield. The step yield can be restored by extending the column load and incorporating a short wash at the end of the load stage. The use of WPC with anion exchange resins enables a two-column cGMP purification platform to be used for many different mAbs. The operating window for WPC can be easily established using high throughput batch-binding screens. Under conditions that favor very strong product binding, competitive effects from product binding can give rise to a reduction in column loading capacity. Robust performance of WPC anion exchange chromatography has been demonstrated in multiple cGMP mAb purification processes. Excellent clearance of host cell proteins, leached Protein A, DNA, high molecular weight species, and model virus has been achieved.     

Development of a modular virus clearance package for anion exchange chromatography operated in weak partitioning mode

Anion exchange chromatography (AEX) operated under weak partitioning mode has been proven to be a powerful polishing step as well as a robust viral clearance step in Pfizer's monoclonal antibody (mAb) platform purification process. A multivariate design of experiment (DoE) study was conducted to understand the impact of operating parameters and feedstream impurity levels on viral clearance by weak partitioning mode AEX. Bacteriophage was used initially as a surrogate for neutral and acidic isoelectric point mammalian viruses (e.g., retrovirus and parvovirus). Five different mAbs were used in the evaluation of process parameters such as load challenge (both product and impurities), load pH, load conductivity, and contact time (bed height and flow‐rate). The operating ranges obtained from phage clearance studies and Pfizer's historical data were used to define an appropriate operating range for a subsequent clearance study with model retrovirus and parvovirus. Both phage and virus clearance evaluations included feedstreams containing different levels of impurities such as high molecular mass species (HMMS), host cell proteins (HCPs), and host cell DNA. For all the conditions tested, over 5 log₁₀ of clearance for both retrovirus and parvovirus was achieved. The results demonstrated that weak partitioning mode AEX chromatography is a robust step for viral clearance and has the potential to be included as part of the modular viral clearance approach. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:750–757, 2015     

Advective hydrogel membrane chromatography for monoclonal antibody purification in bioprocessing

Protein A chromatography is widely employed for the capture and purification of monoclonal antibodies (mAbs). Because of the high cost of protein A resins, there is a significant economic driving force to seek new downstream processing strategies. Membrane chromatography has emerged as a promising alternative to conventional resin based column chromatography. However, to date, the application has been limited to mostly ion exchange flow through (FT) mode. Recently, significant advances in Natrix hydrogel membrane has resulted in increased dynamic binding capacities for proteins, which makes membrane chromatography much more attractive for bind/elute operations. The dominantly advective mass transport property of the hydrogel membrane has also enabled Natrix membrane to be run at faster volumetric flow rates with high dynamic binding capacities. In this work, the potential of using Natrix weak cation exchange membrane as a mAb capture step is assessed. A series of cycle studies was also performed in the pilot scale device (> 30 cycles) with good reproducibility in terms of yield and product purities, suggesting potential for improved manufacturing flexibility and productivity. In addition, anion exchange (AEX) hydrogel membranes were also evaluated with multiple mAb programs in FT mode. Significantly higher binding capacity for impurities (support mAb loads up to 10Kg/L) and 40X faster processing speed were observed compared with traditional AEX column chromatography. A proposed protein A free mAb purification process platform could meet the demand of a downstream purification process with high purity, yield, and throughput. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:974–982, 2015     

The effect of protein a cycle number on the performance and lifetime of an anion exchange polishing step

Most mAb platform purification processes consist of an affinity capture step followed by one or two polishing steps. An understanding of the performance linkages between the unit operations can lead to robust manufacturing processes. In this study, a weak‐partitioning anion‐exchange chromatography polishing step used in a mAb purification process was characterized through high‐throughput screening (HTS) experiments, small‐scale experiments including a cycling study performed on qualified scale‐down models, and large‐scale manufacturing runs. When material from a Protein A column that had been cycled <10× was loaded on the AEX resin, early breakthrough of impurities and premature loss of capacity was observed. As the cycle number on the Protein A resin increased, the capacity of the subsequent AEX step increased. Different control strategies were considered for preventing impurity breakthrough and improving AEX resin lifetimes. Depth filtration of the Protein A peak pool significantly improved the AEX resin capacity, robustness, and lifetime. Further, the turbidity of the Protein A pool has the potential for use as an in‐process control parameter for monitoring the performance of the AEX step. Biotechnol. Bioeng. 2013; 110: 1142–1152. © 2012 Wiley Periodicals, Inc.     

Fouling of an anion exchange chromatography operation in a monoclonal antibody process: Visualization and kinetic studies

Fouling of chromatographic resins over their operational lifetimes can be a significant problem for commercial bioseparations. In this article, scanning electron microscopy (SEM), batch uptake experiments, confocal laser scanning microscopy (CLSM) and small‐scale column studies were applied to characterize a case study where fouling had been observed during process development. The fouling was found to occur on an anion exchange (AEX) polishing step following a protein A affinity capture step in a process for the purification of a monoclonal antibody. Fouled resin samples analyzed by SEM and batch uptake experiments indicated that after successive batch cycles, significant blockage of the pores at the resin surface occurred, thereby decreasing the protein uptake rate. Further studies were performed using CLSM to allow temporal and spatial measurements of protein adsorption within the resin, for clean, partially fouled and extensively fouled resin samples. These samples were packed within a miniaturized flowcell and challenged with fluorescently labeled albumin that enabled in situ measurements. The results indicated that the foulant has a significant impact on the kinetics of adsorption, severely decreasing the protein uptake rate, but only results in a minimal decrease in saturation capacity. The impact of the foulant on the kinetics of adsorption was further investigated by loading BSA onto fouled resin over an extended range of flow rates. By decreasing the flow rate during BSA loading, the capacity of the resin was recovered. These data support the hypothesis that the foulant is located on the particle surface, only penetrating the particle to a limited degree. The increased understanding into the nature of the fouling can help in the continued process development of this industrial example. Biotechnol. Bioeng. 2013; 110:2425–2435. © 2013 Wiley Periodicals, Inc.     

Novel spiking methods developed for anion exchange chromatography operating in a continuous process

Many manufacturers of biopharmaceuticals are moving from batch to continuous processing. While this approach offers advantages over batch processing, demonstration of viral clearance for continuous processes is challenging. Fluctuating output from a continuous process chromatography column results in a nonhomogeneous load for the subsequent column and must be considered when designing viral clearance studies. One approach to clearance studies is to downscale the connected unit operations and introduce virus by in-line spiking. This is challenging to be implemented at the contract research organization performing the clearance study given the complexity of systems and level of expertise required. Alternately, each unit operation could be evaluated in traditional batch mode but the spiking and loading conditions be modified to mimic the variance introduced by the transition between two connected columns. Using a standard chromatography system, we evaluated a flow-through anion exchange chromatography step in a monoclonal antibody (mAb) manufacturing process using five different methods to introduce the virus to the column. Our data show that whether the virus or the mAbs were introduced in concentrated peaks, or as a homogeneous batch, the clearance of mouse minute virus was similar. This study introduces an alternative way to evaluate viral clearance in a continuous process and demonstrates the robustness of anion exchange chromatography unit operating in continuous processing.     

Effects of pH,conductivity, host cell protein,and DNA size distribution on DNA clearance in anion exchange chromatography media

Flowthrough anion exchange chromatography is commonly used as a polishing step in downstream processing of monoclonal antibodies and other therapeutic proteins to remove process‐related impurities and contaminants such as host cell DNA, host cell proteins, endotoxin, and viruses. DNA with a wide range of molecular weight distributions derived from Chinese Hamster Ovary cells was used to advance the understanding of DNA binding behavior in selected anion exchange media using the resin (Toyopearl SuperQ‐650M) and membranes (Mustang® Q and Sartobind® Q) through DNA spiking studies. The impacts of the process parameters pH (6–8), conductivity (2–15 mS/cm), and the potential binding competition between host cell proteins and host cell DNA were studied. Studies were conducted at the least and most favorable experimental conditions for DNA binding based on the anticipated electrostatic interactions between the host cell DNA and the resin ligand. The resin showed 50% higher DNA binding capacity compared to the membrane media. Spiking host cell proteins in the load material showed no impact on the DNA clearance capability of the anion exchange media. DNA size distributions were characterized based on a “size exclusion qPCR assay.” Results showed preferential binding of larger DNA fragments (>409 base pairs). © 2017 The Authors Biotechnology Progress published by Wiley Periodicals, Inc. on behalf of American Institute of Chemical Engineers Biotechnol. Prog., 34:141–149, 2018     

Enrichment of adeno-associated virus serotype 5 full capsids by anion exchange chromatography with dual salt elution gradients

Adeno-associated virus-based gene therapies have demonstrated substantial therapeutic benefit for the treatment of genetic disorders. In manufacturing processes, viral capsids are produced with and without the encapsidated gene of interest. Capsids devoid of the gene of interest, or “empty” capsids, represent a product-related impurity. As a result, a robust and scalable method to enrich full capsids is crucial to provide patients with as much potentially active product as possible. Anion exchange chromatography has emerged as a highly utilized method for full capsid enrichment across many serotypes due to its ease of use, robustness, and scalability. However, achieving sufficient resolution between the full and empty capsids is not trivial. In this work, anion exchange chromatography was used to achieve empty and full capsid resolution for adeno-associated virus serotype 5. A salt gradient screen of multiple salts with varied valency and Hofmeister series properties was performed to determine optimal peak resolution and aggregate reduction. Dual salt effects were evaluated on the same product and process attributes to identify any synergies with the use of mixed ion gradients. The modified process provided as high as ≥75% AAV5 full capsids (≥3-fold enrichment based on the percent full in the feed stream) with near baseline separation of empty capsids and achieved an overall vector genome step yield of >65%.     

Investigating the combination of single-pass tangential flow filtration and anion exchange chromatography for intensified mAb polishing

There is growing interest within the biopharmaceutical industry to improve manufacturing efficiency through process intensification, with the goal of generating more product in less time with smaller equipment. In monoclonal antibody (mAb) purification, a unit operation that can benefit from intensification is anion exchange (AEX) polishing chromatography. Single-pass tangential flow filtration (SPTFF) technology offers an opportunity for process intensification by reducing intermediate pool volumes and increasing product concentration without recirculation. This study evaluated the performance of an AEX resin, both in terms of host cell protein (HCP) purification and viral clearance, following concentration of a mAb feed using SPTFF. Results show that preconcentration of AEX feed material improved isotherm conditions for HCP binding, resulting in a fourfold increase in resin mAb loading at the target HCP clearance level. Excellent clearance of minute virus of mouse and xenotropic murine virus was maintained at this higher load level. The increased mAb loading enabled by SPTFF preconcentration effectively reduced AEX column volume and buffer requirements, shrinking the overall size of the polishing step. In addition, the suitability of SPTFF for extended processing time operation was demonstrated, indicating that this approach can be implemented for continuous biomanufacturing. The combination of SPTFF concentration and AEX chromatography for an intensified mAb polishing step which improves both manufacturing flexibility and process productivity is supported.     

Purification of long helical capsid of newcastle disease virus from Escherichia coli using anion exchange chromatography

NP_Δc375 is a truncated version of the nucleocapsid protein of Newcastle disease virus (NDV) which self‐assembles into a long helical structure. A packed bed anion exchange chromatography (PB‐AEC), SepFastTM Supor Q pre‐packed column, was used to purify NP_Δc375 from clarified feedstock. This PB‐AEC column adsorbed 76.2% of NP_Δc375 from the clarified feedstock. About 67.5% of the adsorbed NP_Δc375 was successfully eluted from the column by applying 50 mM Tris‐HCl elution buffer supplemented with 0.5 M NaCl at pH 7. Thus, a recovery yield of 51.4% with a purity of 76.7% which corresponds to a purification factor of 6.5 was achieved in this PB‐AEC operation. Electron microscopic analysis revealed that the helical structure of the NP_Δc375 purified by SepFast^TM Supor Q pre‐packed column was as long as 490 nm and 22–24 nm in diameter. The antigenicity of the purified NP_Δc375 was confirmed by enzyme‐linked immunosorbent assay. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29: 564–567, 2013     

Structure of the murine anion exchange protein

A full-length clone encoding the mouse erythrocyte anion exchange protein, band 3, has been isolated from a cDNA library using an antibody against the mature erythrocyte protein. The complete nucleotide sequence has been determined. Substantial homology is evident between the deduced murine amino acid sequence and published sequences of fragments of human band 3 protein. The amino-terminal 420 and the carboxy-terminal 32 residues constitute polar, soluble domains, while the intervening 475 amino acids are likely to be intimately associated with the lipid bilayer. Hydrophobic analysis of this sequence, together with structural studies on the human protein, suggests the possibility of at least 12 membrane spans, predicting that both the amino- and carboxy-termini are intracellular.     

Generic/matrix evaluation of SV40 clearance by anion exchange chromatography in flow-through mode

The potential of viral contamination is a regulatory concern for continuous cell line-derived pharmaceutical proteins. Complementary and redundant safety steps, including an evaluation of the viral clearance capacity of unit operations in the purification process, are performed prior to registration and marketing of biotechnology pharmaceuticals. Because process refinement is frequently beneficial, CBER/FDA has published guidance facilitating process improvement by delineating specific instances where the bracketing and generic approaches are appropriate for virus removal validation. In this study, a generic/matrix study was performed using Q-Sepharose Fast Flow (QSFF) chromatography to determine if bracketing and generic validation can be applied to anion exchange chromatography. Key operational parameters were varied to upper and lower extreme values and the impact on viral clearance was assessed using simian virus 40 (SV40) as the model virus. Operational ranges for key chromatography parameters were identified where an SV40 log(10) reduction value (LRV) of >or=4.7 log(10) is consistently achieved. On the basis of the apparent robustness of SV40 removal by Q-anion exchange chromatography, we propose that the concept of "bracketed generic" validation can be applied to this and potentially other chromatography unit operations.     

Sulfate transport in rabbit ileum: Characterization of the serosal border anion exchange process

Summary The preceding paper [30] shows that transepithelial ileal SO₄ transport involves Na-dependent uptake across the ileal brush border, and Cl-dependent efflux across the serosal border. The present study examines more closely the serosal efflux process. Transepithelial mucosa (m)-to-serosa (s) ands-to-m fluxes (J _ms,J _sm) across rabbit ileal mucosa were determined under short-circuit conditions. SO₄ was present at 0.22mm. In standard Cl, HCO₃ Ringer's,J _ms ^SO4 was 81.3±5.3 (1se) andJ _ms ^SO4 was 2.5±0.2 nmol cm^–2 hr^–1 (n=20). Serosal addition of 4-acetamido-4-isothiocyanostilbene-22-disulfonate (SITS), 44-diisothiocyanostilbene-22-disulfonate (DIDS) or 1-anilino-8-naphthalene-sulfonate (ANS) inhibited SO₄ transport, SITS being the most potent. Several other inhibitors of anion exchange in erythrocytes and other cells had no effect on ileal SO₄ fluxes. In contrast to its effect on SO₄ transport, SITS (500 m) did not detectably alter Cl transport.Replacement of all Cl, HCO₃ and PO₄ with gluconate reducedJ _ms ^SO4 by 70% and increasedJ _ms ^SO4 by 400%. A small but significantJ _net ^SO4 remained.J _ms ^SO4 could be increased by addition to the serosal side of Cl, Br, I, NO₃ or SO₄. The stimulatory effect of all these anions was saturable and SITS-inhibitable. The maximalJ _ms ^SO4 in the presence of Cl was considerably higher than in the presence of SO₄ (73.1 and 42.2 nmol. cm^–2 hr^–1, respectively;p<0.001). TheK _1/2 value for Cl was 7.4mm, 10-fold higher than that for SO₄ (0.7mm). Omitting HCO₃ and PO₄ had no measurable effects on SO₄ fluxes.This study shows that (i) SO₄ crosses the serosal border of rabbit ileal mucosa by anion exchange; (ii) the exchange process is inhibited by SITS, DIDS and ANS, but not by several other inhibitors of anion exchange in other systems; (iii) SO₄ may exchange for Cl, Br, I, NO₃ and SO₄ itself, but probably not for HCO₃ or PO₄; (iv) kinetics of the exchange system suggest there is a greater affinity for SO₄ than for Cl, although the maximal rate of exchange is higher in the presence of Cl; and, finally (v) SITS has little or no effect on net Cl transport.     

The impact of protein exclusion on the purity performance of ion exchange resins

Dynamic binding capacity (DBC) decreases with increasing conductivity in the equilibrium regime for ion exchange chromatography. An exclusion regime has been demonstrated in ion exchange resins where DBC increases with increasing conductivity and decreasing protein charge. The purpose of this work was to examine the impact of the exclusion regime on impurity removal. Resin performance was evaluated based on dynamic binding capacities and purity within the exclusion and equilibrium regimes. The results revealed that Chinese hamster ovary proteins (CHOP), a major impurity, exhibit similar exclusion trends as the MAb proteins. The results further the understanding of the exclusion regime and its impact on product purity, a critical area for IEX development and optimization.     

Artifact-inducing enrichment of ethylenediaminetetraacetic acid and ethyleneglycoltetraacetic acid on anion exchange resins

Multivalent metal chelators, ethylenediaminetetraacetic acid (EDTA) and ethyleneglycoltetraacetic acid (EGTA), are used extensively during protein purification. Both strong (Q) and weak (DEAE) anion exchange resins were found to adsorb surprisingly large quantities of EDTA and EGTA that elute from the resin at NaCl concentrations of approximately 240 mM (EDTA) and 140 mM (EGTA). The EDTA/EGTA elution and saturation parameters were determined for five commonly used anion exchange resins. The resulting concentration of eluted EDTA was 10- to 200-fold higher than that originally present in the sample or in the mobile phase. Samples from fractions containing such a high concentration of EDTA were found to inhibit Mg²⁺-dependent polymerase chain reaction (PCR). EDTA binding to the anion exchange resins could saturate the resin, decrease its binding capacity, and displace weakly bound proteins such as green fluorescent protein (GFP). Several steps are suggested to minimize on-column EDTA concentration, including column equilibration in the absence of any EDTA, lower concentrations (0.1–0.5 mM) of EDTA, monitoring eluate absorbance at 280 nm as well as at 215 nm, adding EDTA back into fractions eluting before the EDTA peak, and performing blank column runs to control for the effect of changes in EDTA concentration in downstream assays.     

Efficient and easily scalable protein folding strong anion exchange chromatography for renaturation and simultaneous purification of recombinant human asparaginase from E. coli

Recombinant proteins are revolutionizing present day therapeutics. They are generally expressed as insoluble inclusion bodies in the E. coli and mis‐folding, loss of protein, and high cost of down streaming are the hurdles in their recovery. For the first time, we are reporting the refolding with simultaneous purification of rhASP in E. coli using a single step utilizing protein folding‐strong anion exchange chromatography (PF‐SAX). The purification method is also standardized for optimal concentration of solution additives, pH, and mobile phase composition. The results showed purification of rhASP with anion exchange chromatography was effective. Phosphate buffer and slightly alkaline pH produced significant recovery yields and purity profiles. The effect of solution additives such as arginine, glycerol, TMAO, sorbitol, dextran, glutamate, and fructose on rhASP renaturation is also investigated. Significant results were achieved using arginine‐TMAO combination in terms of purity, recovery yield and specific activity of 99%, 78%, and 210 IU/mg, respectively. The work concludes that PF‐SAX refolding method is superior to other conventional methods and it can be applied to large scale purification of rhASP produced in E. coli. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:1036–1044, 2018     

Comparison of theN-glycoloylneuraminic andN-acetylneuraminic acid content of platelets and their precursors using high performance anion exchange chromatography

N-Acetylneuraminic acid (Neu5Ac) andN-glycoloylneuraminic acid (Neu5Gc) are distributed widely in nature. Using a Carbopac PA-1 anion exchange column, we have determined the ratios of Neu5Ac and Neu5Gc in hydrolysates of platelets and their precursors: a rat promegakaryoblastic (RPM) cell line and a human megakaryoblastic leukemia cell line (MEG-01). The ratio of Neu5Gc:Neu5Ac in cultured RPM cells is 16:1, whereas in platelet rich plasma and cultured MEG-01 cells it is 1:38 and 1:28, respectively. The nature of these sialic acids from RPM cells was verified using thin layer chromatography and liquid secondary ion mass spectrometry. The relevance of increased Neu5Gc levels in early stages of development is discussed.Abbreviations Neu5Ac N-acetylneuraminic acid - Neu5Gc N-glycoloylneuraminic acid - RPM rat promegakaryoblast - MEG-01 human megakaryoblastic leukaemia cell line - PAD pulsed amperometric detection - WGA wheat germ agglutinin - FCS foetal calf serum - PPEADF phosphatidylethanolamine dipalmitoyl - LSIMS liquid secondary ion mass spectrometry - HPAEC high performance anion exchange chromatography - TBA thiobarbituric acid