Computational designing of the ligands of Protein L affinity chromatography based on molecular docking and molecular dynamics simulations

Protein L is a multidomain protein from Peptostreptococcus magnus with binding affinity to kappa light chain of human immunoglobulin (Ig) which is used for the purification of antibody fragments by affinity chromatography. The advances in protein engineering and computational biology approaches lead to the development of engineered affinity ligands with improved properties including binding affinity. In this study, molecular dynamics simulations (MDs) and Osprey software were used to design single B domains of the Protein L with higher affinity to antibody fragments. The modified B domains were then polymerized to ligand with six B domains by homology modeling methods. The results showed that single B domain mutants of MB1 (Thr865Trp) and MB2 (Thr847Met-Thr865Trp) had higher binding affinity to Fab compared to the wild single B domain. Also, MDs and molecular docking results showed that the polymerized Proteins L including the wild and mutated six B domains (6B0, 6B1, and 6B2) were stable during MDs and the two mutants of 6B1 and 6B2 showed higher binding affinity to Fab relative to the wild type.Communicated by Ramaswamy H. Sarma.

Complementary methods for monitoring hole-hole homodimer associated with a WuXiBody-based asymmetric bispecific antibody

WuXiBody is a bispecific antibody (bsAb) platform developed by WuXi Biologics. Its key feature is the replacement of one parental antibody's CH1/CL region with the T-cell receptor (TCR) constant domain, which prevents mispairing between non-cognate heavy chain and light chain. In addition, heavy chain heterodimerization in asymmetric WuXiBody molecule is promoted by the knobs-into-holes (KiH) technology. Despite the great success of KiH strategy in improving heterodimer formation, homodimers (especially the hole-hole homodimer) can still be generated at low levels. In general, detection and monitoring of homodimers during KiH bsAb purification are challenging as homodimers share similar physicochemical properties with the target heterodimeric bsAb. Nevertheless, the unique design of WuXiBody allows homodimers to be effectively detected and monitored by multiple methods. In the current work, with an asymmetric WuXiBody case study, we demonstrated that hole-hole homodimer can be effectively monitored by six chromatography methods including hydrophobic interaction chromatography (HIC), reversed phase (RP), cation exchange (CEX), KappaSelect, CaptureSelect CH1-XL and Protein L.

Immunoglobulin-binding protein-based affinity chromatography in bispecific antibody purification: Functions beyond product capture

In general, purification of bispecific antibody (bsAb) is more challenging than that of monospecific antibody due to the increased complexity in byproduct profile. Like in the case of monospecific antibody purification, immunoglobulin-binding protein-based affinity chromatography is an indispensable tool for bsAb purification. For example, Protein A affinity chromatography has been widely used to capture Fc-containing bsAbs whereas other affinity media such as Protein L and KappaSelect, which bind kappa light chain, are used to capture bsAbs that do not contain a Protein A-binding site. In fact, affinity chromatography also possesses the capability of removing certain product-related impurities in bsAb purification when it is conducted with suitable medium and under appropriate conditions. Fully exploring the potential of affinity chromatography in bsAb purification to achieve both product capture and byproduct removal is highly desirable, as this can greatly alleviate the purification burden on subsequent polishing steps and hence improves the overall robustness of the downstream process. This article briefly reviews the byproduct clearance potential of several commonly used affinity media under relevant bsAb purification scenarios.

Three-dimensional chromatography for purification and characterization of antibody fragments and related impurities from Escherichia coli crude extracts

Antibody fragments (Fab) are often produced by recombinant methods in Escherichia coli as no glycosylation is needed. Besides the correctly expressed Fab molecule, a multitude of host cell impurities and product related impurities are present in the crude sample. The identification and characterization of the product-related impurities, such as modified Fab-molecules or free light chain, are of utmost importance. The objective of this work was to design a purification strategy to isolate and characterize Fab and related impurities. A three-dimensional chromatography method was established, consisting of two affinity steps (Protein G and Protein L) and subsequent cation exchange chromatography, followed by mass spectrometry analysis of the purified samples. The procedure was automated by collecting the eluted target species in loops and directly loading the samples onto the high-resolution cation exchange chromatography column. As an example, four different Fab molecules are characterized. All four samples contained mainly the correct Fab, while only one showed extensive N-terminal pyroglutamate formation of the Fab. In another case, we found a light chain variant with uncleaved amino acids from the lead molecule, which was not used for the formation of whole Fab as only correct Fab was found in that sample. Impurities with lower molecular weights, which were bound on the Protein L column, were observed in all samples, and identified as fragments of the light chain. In conclusion, we have devised a platform for characterizing Fab and Fab-related impurities, which significantly facilitated strain selection and optimization of cultivation conditions.

Impact of salt concentration in mobile phase on antibody retention in Protein A, Protein L and KappaSelect affinity chromatography

Protein A, Protein L and KappaSelect affinity resins have been widely used for antibody purification. Elution of antibody bound to these resins is typically achieved by acidic pH. In addition, elution can be moderately adjusted by tuning the salt concentration in mobile phase as hydrophobic interactions play a major role in binding. In this study, we assessed the impact of salt concentration in mobile phase on antibody retention in these three types of affinity chromatography. The data suggest that salt concentration has a bigger impact on retention in the two light chain-binding affinity columns (i.e., Protein L and KappaSelect) than in Protein A column. In particular, lowering salt concentration in mobile phase for Protein L and KappaSelect columns allows elution become feasible at higher pH. In addition, this finding suggests that wash in these two types of column aimed at removing weakly-bound byproducts can also be performed at increased pH by lowering salt concentration in the wash buffer. Rendering wash and elution feasible at higher pH has practical value for cases where the target antibodies are sensitive to stringent conditions.

Controlled conductivity at low pH in Protein L chromatography enables separation of bispecific and other antibody formats by their binding valency

The complex molecular formats of recent therapeutic antibodies, including bispecific antibodies, antibody fragments, and other fusion proteins, makes the task of purifying the desired molecules in a limited number of purification steps more and more challenging. Manufacturing these complicated biologics can be substantially improved in the affinity capture stage if the simple bind-and-elute mode is accompanied by targeted removal of the impurities, such as mis-paired antibodies and oligomers or aggregates. Here, we report a method, based on the binding valency to Protein L resin, of separating proteins during the elution step by simply controlling the conductivity at low pH. We show that the method efficiently separated targeted antibodies from mis-paired and aggregated species. Notably, the number of Protein L binding sites can be built into the molecule by design to facilitate the purification. This method may be useful for purifying various antibody formats at laboratory and manufacturing scales.

Antibody Fragments Humanization: Beginning with the End in Mind

Molecular engineering has made possible to reformat monoclonal antibodies into smaller antigen-binding structures like scFvs, diabodies, Fabs with new potential in vivo applications because they do not induce Fc-mediated functions. However, most of these molecules are from rodent origin. As a consequence, they are immunogenic and approval for administration to humans requires prior humanization. Today, there is no well-identified strategy to create recombinant humanized antibody V-domains that preserve the antigen-binding characteristics of the parental antibody associated with high stability and solubility. Here, we propose a strategy that consists in grafting CDRs onto properly chosen human antibody frameworks in order to reduce immunogenicity. A flowchart indicates the way to proceed in order to introduce an internal affinity purification tag while structural refinements are proposed to maintain antigen-binding characteristics. The best humanized candidates are identified through selection steps including in silico analysis, research scale production followed by early functional evaluation, purification assays, aggregation, and stability assessment.

Purification of Antibodies Using Affinity Chromatography

Affinity chromatography permits the isolation of a target analyte from a complex mixture and can be utilized to purify proteins, carbohydrates, drugs, haptens, or any analyte of interest once an affinity pair is available. It involves the exploitation of specific interactions between a binding affinity pair, such as those between an antibody and its associated antigen, or between any ligand and its associated binding receptor/protein. With the discovery of protein A in 1970, and, subsequently protein G and L, immuno-affinity chromatography has grown in popularity and is now the standard methodology for the purification of antibodies which may be implemented for a selection of different applications such as immunodiagnostics. This chapter is designed to inform the researcher about the basic techniques involved in the affinity chromatography-based purification of monoclonal, polyclonal, and recombinant antibodies. Examples are provided for the use of protein A and G. In addition, tables are provided that allow the reader to select the most appropriate protein for use in the isolation of their antibody.

Fc-Binding Ligands of Immunoglobulin G: An Overview of High Affinity Proteins and Peptides

The rapidly increasing application of antibodies has inspired the development of several novel methods to isolate and target antibodies using smart biomaterials that mimic the binding of Fc-receptors to antibodies. The Fc-binding domain of antibodies is the primary binding site for e.g., effector proteins and secondary antibodies, whereas antigens bind to the Fab region. Protein A, G, and L, surface proteins expressed by pathogenic bacteria, are well known to bind immunoglobulin and have been widely exploited in antibody purification strategies. Several difficulties are encountered when bacterial proteins are used in antibody research and application. One of the major obstacles hampering the use of bacterial proteins is sample contamination with trace amounts of these proteins, which can invoke an immune response in the host. Many research groups actively develop synthetic ligands that are able to selectively and strongly bind to antibodies. Among the reported ligands, peptides that bind to the Fc-domain of antibodies are attractive tools in antibody research. Besides their use as high affinity ligands in antibody purification chromatography, Fc-binding peptides are applied e.g., to localize antibodies on nanomaterials and to increase the half-life of proteins in serum. In this review, recent developments of Fc-binding peptides are presented and their binding characteristics and diverse applications are discussed.

Bio-nanocapsules displaying various immunoglobulins as an active targeting-based drug delivery system

The bio-nanocapsule (BNC) is an approximately 30-nm particle comprising the hepatitis B virus (HBV) envelope L protein and a lipid bilayer. The L protein harbors the HBV-derived infection machinery; therefore, BNC can encapsulate payloads such as drugs, nucleic acids, and proteins and deliver them into human hepatocytes specifically in vitro and in vivo. To diversify the possible functions of BNC, we generated ZZ-BNC by replacing the domain indispensable for the human hepatotrophic property of BNC (N-terminal region of L protein) with the tandem form of the IgG Fc-binding Z domain of Staphylococcus aureus protein A. Thus, the ZZ-BNC is an active targeting-based drug delivery system (DDS) nanocarrier that depends on the specificity of the IgGs displayed. However, the Z domain limits the animal species and subtypes of IgGs that can be displayed on ZZ-BNC. In this study, we introduced into BNC an Ig κ light chain-binding B1 domain of Finegoldia magna protein L (protein-L B1 domain) and an Ig Fc-binding C2 domain of Streptococcus species protein G (protein-G C2 domain) to produce LG-BNC. The LL-BNC was constructed in a similar way using a tandem form of the protein-L B1 domain. Both LG-BNC and LL-BNC could display rat IgGs, mouse IgG1, human IgG3, and human IgM, all of which not binding to ZZ-BNC, and accumulate in target cells in an antibody specificity-dependent manner. Thus, these BNCs could display a broad spectrum of Igs, significantly improving the prospects for BNCs as active targeting-based DDS nanocarriers.

STATEMENT OF SIGNIFICANCE

We previously reported that ZZ-BNC, bio-nanocapsule deploying the IgG-binding Z domain of protein A, could display cell-specific antibody in an oriented immobilization manner, and act as an active targeting-based DDS nanocarrier. Since the Z domain can only bind to limited types of Igs, we generated BNCs deploying other Ig-binding domains: LL-BNC harboring the tandem form of Ig-binding domain of protein L, and LG-BNC harboring the Ig binding domains of protein L and protein G sequentially. Both BNCs could display a broader spectrum of Igs than does the ZZ-BNC. When these BNCs displayed anti-CD11c IgG or anti-EGFR IgG, both of which cannot bind to Z domain, they could bind to and then enter their respective target cells.

Treatment of murine mast cells with IgEκ and protein L enhances apoptotic cell death induced by IL-3 withdrawal

Engagement of the high-affinity IgE receptor (FcεRI) can be either protective or non-protective against apoptotic cell death (ACD) in bone marrow-derived murine mast cells (BMMCs) after IL-3 withdrawal, depending on the avidity between IgE and its antigen. We recently reported that protein L (PpL), a bacterial Igκ-binding soluble protein, is able to stimulate intracellular signaling to induce activation of BMMCs by interacting with the IgEκ-FcεRI complex. However, it is unclear if cross-linking of FcεRI with IgEκ and PpL prevents or enhances IL-3-dependent ACD in BMMCs. In the present study, we found that IL-3-dependent ACD of BMMCs is accelerated by loading soluble PpL in the presence of IgEκ-occupied FcεRIα. For this purpose, soluble PpL was incorporated into the BMMCs. Unlike soluble PpL, immobilized PpL failed to enhance ACD, although both forms of PpL induced IL-6 production equally in BMMCs. In addition, we observed that DNS5-BSA protected anti-DNS IgE-sensitized BMMCs from IL-3 depletion-mediated ACD by inducing the production of autocrine IL-3. In contrast, DNS5-PpL enhanced IL-3 withdrawal-induced ACD of anti-DNS IgE-sensitized BMMCs and reduced the production of autocrine IL-3. These findings suggest that PpL increases IL-3 withdrawal-induced ACD of IgEκ-sensitized BMMCs by incorporating PpL into the BMMCs and that this internalized PpL may interfere with survival signals via FcεRI.