Differential binding of heavy chain variable domain 3 antigen binding fragments to protein a chromatography resins

Removal of homodimer species with MabSelect VH3 during the purification of an asymmetric bispecific antibody

By-products are continuously generated during the manufacturing process of bispecific antibodies, among which homodimers represent the most critical impurity. The effective removal of homodimers is essential, as their presence compromises product purity and may adversely affect therapeutic safety and efficacy. Affinity chromatography, which exploits the highly selective molecular interactions between target antibodies and immobilized ligands, remains the gold-standard purification technique for monoclonal (mAbs) and bispecific antibodies (bsAbs). In this study, we evaluated the separation efficiency of homodimers using three commercially available Protein A resins with distinct binding sites: MabSelect PrismA, MabSelect SuRe LX, and MabSelect VH3. Both the Fc and VH3 regions of the bispecific antibodies (bsAbs) and homodimers in this study have different binding capacities to the affinity resin. Comparative analysis revealed that MabSelect VH3, which relies exclusively on VH3 domain interactions, achieved the highest separation performance with final product purity exceeding 98.9 %. In contrast to MabSelect SuRe LX's single Fc-binding mechanism, separation efficiency was compromised by MabSelect PrismA's dual-binding (Fc and VH3) interactions. Additionally, the differential Fc affinities were identified as the dominant factor influencing resolution under concurrent Fc-binding and VH3 domain disparities between the bsAb and homodimer. These findings provide valuable insights for downstream process optimization in bsAb production, emphasizing the importance of strategic resin selection based on molecular interaction mechanisms.

An inert tracer: The binding site of a fluorescent dye on the antibody and its effects on Protein A chromatography

Fluorescently labeled antibodies are widely used to visualize the adsorption process in protein chromatography using confocal laser scanning microscopy (CLSM), but also as a tracer for determination of residence time distribution (RTD) in continuous chromatography. It is assumed that the labeled protein is inert and representative of the unlabeled antibody, ignoring the fact that labeling with a fluorescent dye can change the characteristics of the original molecule. It became evident that the fluorescently labeled antibody has a higher affinity toward protein A resins such as MabSelect Sure. This can be due to slight differences in hydrophobicity and net charge, which are caused by the addition of the fluorescent dye. However, this difference is eliminated when using high salt concentrations in the adsorption studies. In this work, the site occupancy of two labeled antibodies, MAb1 (IgG1 subclass) and MAb2 (IgG2 subclass) conjugated with the fluorescent dye Alexa Fluor™ 488 was elucidated by intact mass spectrometry (MS) and peptide mapping LC-MS/MS, employing a sequential cleavage with Endoproteinase Lys-C and trypsin and in parallel with chymotrypsin alone. It was shown that the main binding site for the dye was a specific lysine in the heavy chains of the MAb1 and MAb2 molecules, in positions 188 and 189 respectively. Other lysine residues distributed throughout the protein sequence were labeled to a lot lesser extent. The labeled antibody had a slightly different affinity to MabSelect Sure although its primary binding site (to Protein A) was not affected by labeling, despite the secondary region responsible for binding to the protein A was partly labeled. Overall, the fluorescent-labeled antibodies are a good compromise as an inert tracer in residence time distribution and chromatography studies because they are much cheaper than isotope-labeled antibodies; However, the differences between the labeled and unlabeled antibodies should be considered.

Mixed-mode size-exclusion silica resin for polishing human antibodies in flow-through mode

The polishing step in the downstream processing of therapeutic antibodies removes residual impurities from Protein A eluates. Among the various classes of impurities, antibody fragments are especially challenging to remove due to the broad biomolecular diversity generated by a multitude of fragmentation patterns. The current approach to fragment removal relies on ion exchange or mixed-mode adsorbents operated in bind-and-gradient-elution mode. However, fragments that bear strong similarity to the intact product or whose biophysical features deviate from the ensemble average can elude these adsorbents, and the lack of a chromatographic technology enabling robust antibody polishing is recognized as a major gap in downstream bioprocessing. Responding to this challenge, this study introduces size-exclusion mixed-mode (SEMM) silica resins as a novel chromatographic adsorbent for the capture of antibody fragments irrespective of their biomolecular features. The pore diameter of the silica beads features a narrow distribution and is selected to exclude monomeric antibodies, while allowing their fragments to access the pores where they are captured by the mixed-mode ligands. The static and dynamic binding capacity of the adsorbent ranged respectively between 30-45 and 25-33 gs of antibody fragments per liter of resin. Selected SEMM-silica resins also demonstrated the ability to capture antibody aggregates, which adsorb on the outer layer of the beads. Optimization of the SEMM-silica design and operation conditions - namely, pore size (10 nm) and ligand composition (quaternary amine and alkyl chain) as well as the linear velocity (100 cm/h), ionic strength (5.7 mS/cm), and pH (7) of the mobile phase - afforded a significant reduction of both fragments and aggregates, resulting into a final antibody yield up to 80% and monomeric purity above 97%.

Different VH3-binding Protein A Resins Show Comparable VH3-binding Mediated Byproduct Separation Capabilities Despite Having Varied Dynamic Binding Capacities Towards A VH3 Fab

BACKGROUND

Protein A resins have been widely used for product capture during mAb, bispecific antibody (bsAb), and Fc-fusion protein purification. While Protein A ligands mainly bind the Fc region, many of them can also bind the VH3 domain. During mAb/bsAb purification, certain truncated byproducts may contain the same Fc region as the product but fewer numbers of the VH3 domain. In such a scenario, VH3-binding Protein A resins provide a potential means for byproduct separation based on the difference in VH3-binding valency. As the ligands of different VH3-binding Protein A resins are derived from distinct domains of the native Protein A, it would be interesting to know whether they possess comparable capabilities for separating species with the same Fc region but different numbers of VH3 domain.

OBJECTIVE

This study aims to explore the potential of different VH3-binding Protein A resins for separating antibody species with the same Fc region but different numbers of VH3 domain.

METHODS

The VH3 Fab was released from a VH3-containing mAb by papain digestion. Post digestion, the released VH3 Fab was purified sequentially using CaptureSelect CH1-XL and MabSelect SuRe affinity chromatography. The purified VH3 Fab was used as the load material to assess the dynamic binding capacity (DBC) of five VH3-binding Protein A resins (i.e., Amshpere A3, Jetted A50, MabCaptureC, MabSelect and MabSelect PrismA). The potential of VH3-binding Protein A resins for separating species having the same Fc region but different numbers of VH3 domain was evaluated using an artificial mixture composed of the product and a truncated byproduct, which contained one and zero VH3 domain, respectively (both species contained the same Fc region). Sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) was used to monitor Fab purification and separation of species containing the same Fc region but different numbers of VH3 domain.

RESULTS

When loaded with an isolated VH3 Fab, different VH3-binding Protein A resins showed varied DBCs. Nevertheless, when these Protein A resins were used to separate a truncated byproduct, which contained the Fc region only without any VH3 domain, from the product, which included one VH3 domain in addition to the Fc region, they showed comparable capabilities for separating these two species.

CONCLUSION

Although different VH3-binding Protein A resins showed varied DBCs towards a VH3 Fab, they exhibited comparable capabilities for separating species with the same Fc region but different numbers of VH3 domain.

Protein A does not induce allosteric structural changes in an IgG1 antibody during binding

Affinity chromatography is widely used for antibody purification in biopharmaceutical production. Although there is evidence suggesting that affinity chromatography might induce structural changes in antibodies, allosteric changes in structure have not been well-explored. Here, we used hydrogen exchange-mass spectrometry (HX-MS) to reveal conformational changes in the NIST mAb upon binding with a protein A (ProA) matrix. HX-MS measurements of NIST mAb bound to in-solution and resin forms of ProA revealed regions of the C_H2 and C_H3 domains with increased protection from HX upon ProA binding, consistent with the known ProA binding region. In-solution ProA experiments revealed regions in the F_ab with increased HX uptake when the ProA:mAb molar ratio was increased to 2:1, suggesting an allosterically induced increase in backbone flexibility. Such effects were not observed with lower ProA concentration (1:1 molar ratio) or when ProA resin was used, suggesting some kind of change in binding mode. Since all pharmaceutical processes use ProA bound to resin, our results rule out reversible allosteric effects on the NIST mAb during interaction with resin ProA. However, irreversible effects cannot be ruled out since the NIST mAb was previously exposed to ProA during its original purification.

A bispecific IgG format containing four independent antigen binding sites

Bispecific antibodies come in many different formats, including the particularly interesting two-in-one antibodies, where one conventional IgG binds two different antigens. The IgG format allows these antibodies to mediate Fc-related functionality, and their wild-type structure ensures low immunogenicity and enables standard methods to be used for development. It is however difficult, time-consuming and costly to generate two-in-one antibodies. Herein we demonstrate a new approach to create a similar type of antibody by combining two different variable heavy (VH) domains in each Fab arm of an IgG, a tetra-VH IgG format. The VHs are used as building blocks, where one VH is placed at its usual position, and the second VH replaces the variable light (VL) domain in a conventional IgG. VH domains, binding several different types of antigens, were discovered and could be rearranged in any combination, offering a convenient "plug and play" format. The tetra-VH IgGs were found to be functionally tetravalent, binding two antigens on each arm of the IgG molecule simultaneously. This offers a new strategy to also create monospecific, tetravalent IgGs that, depending on antigen architecture and mode-of-action, may have enhanced efficacy compared to traditional bivalent antibodies.

Homogenous Scavenging Resolves Low-Purification Yield/Selectivity Caused by Secondary Binding of Protein-A to Antigen-Binding Antibody Fragments

Antigen-binding fragments of antibodies are biotechnologically useful agents for decorating drug delivery systems, for blocking cell-surface receptors in cell culture, for recognizing analytes in biosensors, and potentially as therapeutics. They are typically produced by enzymatic digestion of full antibodies and isolated from the undesirable fragment crystallizable (Fc) by affinity chromatography using Protein-A columns. However, while Protein-A has a strong "classical" interaction with Fc fragments, it can also more weakly bind to an "alternative" site on the heavy chain variable region of antigen-binding fragments. As such, purifying small amounts of antibody fragments by Protein-A chromatography can result in low yield. Moreover, loading larger amounts of antibody fragments onto a Protein-A column can result in poor separation, because of competition of Fc and antigen-binding fragments for immobilized Protein-A. This study demonstrates that Protein-A-based homogeneous scavenging resolves this issue by precisely controlling the stoichiometry of Protein-A to Fc fragments, something that is not possible for conventional flow-type systems, such as affinity chromatography.

Single-step Protein A and Protein G avidity purification methods to support bispecific antibody discovery and development

Heavy chain (Hc) heterodimers represent a majority of bispecific antibodies (bsAbs) under clinical development. Although recent technologies achieve high levels of Hc heterodimerization (HD), traces of homodimer contaminants are often present, and as a consequence robust purification techniques for generating highly pure heterodimers in a single step are needed. Here, we describe two different purification methods that exploit differences in Protein A (PA) or Protein G (PG) avidity between homo- and heterodimers. Differential elution between species was enabled by removing PA or PG binding in one of the Hcs of the bsAb. The PA method allowed the avidity purification of heterodimers based on the VH3 subclass, which naturally binds PA and interferes with separation, by using a combination of IgG3 Fc and a single amino acid change in VH3, N82aS. The PG method relied on a combination of three mutations that completely disrupts PG binding, M428G/N434A in IgG1 Fc and K213V in IgG1 CH1. Both methods achieved a high level of heterodimer purity as single-step techniques without Hc HD (93–98%). Since PA and PG have overlapping binding sites with the neonatal Fc receptor (FcRn), we investigated the effects of our engineering both in vitro and in vivo. Mild to moderate differences in FcRn binding and Fc thermal stability were observed, but these did not significantly change the serum half-lives of engineered control antibodies and heterodimers. The methods are conceptually compatible with various Hc HD platforms such as BEAT® (Bispecific Engagement by Antibodies based on the T cell receptor), in which the PA method has already been successfully implemented.