High‐efficiency affinity precipitation of multiple industrial mAbs and Fc‐fusion proteins from cell culture harvests using Z‐ELP‐E2 nanocages

Affinity precipitation using Z‐elastin‐like polypeptide‐functionalized E2 protein nanocages has been shown to be a promising alternative to Protein A chromatography for monoclonal antibody (mAb) purification. We have previously described a high‐yielding, affinity precipitation process capable of rapidly capturing mAbs from cell culture through spontaneous, multivalent crosslinking into large aggregates. To challenge the capabilities of this technology, nanocage affinity precipitation was investigated using four industrial mAbs (mAbs A–D) and one Fc fusion protein (Fc A) with diverse molecular properties. A molar binding ratio of 3:1 Z:mAb was sufficient to precipitate >95% mAb in solution for all molecules evaluated at ambient temperature without added salt. The effect of solution pH on aggregation kinetics was studied using a simplified two‐step model to investigate the protein interactions that occur during mAb–nanocage crosslinking and to determine the optimal solution pH for precipitation. After centrifugation, the pelleted mAb–nanocage complex remained insoluble and was capable of being washed at pH ≥ 5 and eluted with at pH < 4 with >90% mAb recovery for all molecules. The four mAbs and one Fc fusion were purified from cell culture using optimal process conditions, and >94% yield and >97% monomer content were obtained. mAb A–D purification resulted in a 99.9% reduction in host cell protein and >99.99% reduction in DNA from the cell culture fluids. Nanocage affinity precipitation was equivalent to or exceeded expected Protein A chromatography performance. This study highlights the benefits of nanoparticle crosslinking for enhanced affinity capture and presents a robust platform that can be applied to any target mAb or Fc‐containing proteins with minimal optimization of process parameters.     

Design and characterization of novel dual Fc antibody with enhanced avidity for Fc receptors

Monoclonal antibodies (mAbs) have become an important class of therapeutics, particularly in the realm of anticancer immunotherapy. While the two antigen-binding fragments (Fabs) of an mAb allow for high-avidity binding to molecular targets, the crystallizable fragment (Fc) engages immune effector elements. mAbs of the IgG class are used for the treatment of autoimmune diseases and can elicit antitumor immune functions not only by several mechanisms including direct antigen engagement via their Fab arms but also by Fab binding to tumors combined with Fc engagement of complement component C1q and Fcγ receptors. Additionally, IgG binding to the neonatal Fc receptor (FcRn) allows for endosomal recycling and prolonged serum half-life. To augment the effector functions or half-life of an IgG1 mAb, we constructed a novel “2Fc” mAb containing two Fc domains in addition to the normal two Fab domains. Structural and functional characterization of this 2Fc mAb demonstrated that it exists in a tetrahedral-like geometry and retains binding capacity via the Fab domains. Furthermore, duplication of the Fc region significantly enhanced avidity for Fc receptors FcγRI, FcγRIIIa, and FcRn, which manifested as a decrease in complex dissociation rate that was more pronounced at higher densities of receptor. At intermediate receptor density, the dissociation rate for Fc receptors was decreased 6- to 130-fold, resulting in apparent affinity increases of 7- to 42-fold. Stoichiometric analysis confirmed that each 2Fc mAb may simultaneously bind two molecules of FcγRI or four molecules of FcRn, which is double the stoichiometry of a wild-type mAb. In summary, duplication of the IgG Fc region allows for increased avidity to Fc receptors that could translate into clinically relevant enhancement of effector functions or pharmacokinetics.     

Characterization of a unique IgG1 mAb CEX profile by limited Lys-C proteolysis/CEX separation coupled with mass spectrometry and structural analysis

The unique cation exchange chromatography (CEX) charge variant profile of mAb1 is characterized by a combination of mass spectrometry, limited Lys-C digestion followed by CEX separation and structural analysis. During CEX method development, mAb1 showed several unexpected phenomena, including a unique profile containing two main species (acidic 2 and main) and significant instability during stability studies of the main species. Reduced Lys-C peptide mapping identified a small difference in one of the heavy chain peptides (H4) in acidic 2 and further mass analysis identified this difference as Asn55 deamidation. However, the amount of Asn55 deamidation in acidic 2 could account for only half of the species present in this peak. Lys-C limited digest followed by CEX separated several unique peaks in the acidic peak 2 including two pre Fab peaks (LCC1 and LCC2). Whole protein mass analysis suggested that both LCC1 and LCC2 were potentially deamidated species. Subsequent peptide mapping with MS/MS determined that LCC1 contained isoAsp55 and LCC2 contained Asp55. Combining LCC1 and LCC2 CEX peak areas could account for nearly all of the species present in acidic peak 2. Subsequent detailed sequence analysis combined with molecular modeling identified Asn55 and its surrounding residues are responsible for the different CEX behavior and instability of mAb1 following forced degradation at high pH. Overall, the combinatorial approach used in this study proved to be a powerful tool to understand the unique charge variant and stability profile of a monoclonal antibody.     

Competing aggregation pathways for monoclonal antibodies

Aggregation is mediated by local unfolding to allow aggregation “hot spot(s)” to become solvent exposed and available to associate with a hot spot on another partially unfolded protein. Historically, the unfolding of either the crystallizable fragment (Fc) or the antigen binding fragment (Fab) regions of a given monoclonal antibody (MAb) has been implicated in aggregation, with differing results across different proteins. The present work focuses on separately quantifying the aggregation kinetics of isolated Fc, isolated Fab, and intact MAb as a function of pH under accelerated (high temperature) conditions. The results show that both Fab and Fc are aggregation prone and compete within the same MAb.     

A stable engineered human IgG3 antibody with decreased aggregation during antibody expression and low pH stress

Human IgG comprises four subclasses with different biological functions. The IgG3 subclass has a unique character, exhibiting high effector function and Fab arm flexibility. However, it is not used as a therapeutic drug owing to an enhanced susceptibility to proteolysis. Antibody aggregation control is also important for therapeutic antibody development. To date, there have been few reports of IgG3 aggregation during protein expression and the low pH conditions needed for purification and virus inactivation. This study explored the potential of IgG3 antibody for therapeutics using anti‐CD20 IgG3 as a model to investigate aggregate formation. Initially, anti‐CD20 IgG3 antibody showed substantial aggregate formation during expression and low pH treatment. To circumvent this phenomenon, we systematically exchanged IgG3 constant domains with those of IgG1, a stable IgG. IgG3 antibody with the IgG1 CH3 domain exhibited reduced aggregate formation during expression. Differential scanning calorimetric analysis of individual amino acid substitutions revealed that two amino acid mutations in the CH3 domain, N392K and M397V, reduced aggregation and increased CH3 transition temperature. The engineered human IgG3 antibody was further improved by additional mutations of R435H to obtain IgG3KVH to achieve protein A binding and showed similar antigen binding as wild‐type IgG3. IgG3KVH also exhibited high binding activity for FcγRIIIa and C1q. In summary, we have successfully established an engineered human IgG3 antibody with reduced aggregation during bioprocessing, which will contribute to the better design of therapeutic antibodies with high effector function and Fab arm flexibility.     

Investigation of degradation processes in IgG1 monoclonal antibodies by limited proteolysis coupled with weak cation-exchange HPLC

A new cation-exchange high-performance liquid chromatography (HPLC) method that separates fragment antigen-binding (Fab) and fragment crystallizable (Fc) domains generated by the limited proteolysis of monoclonal antibodies (mAbs) was developed. This assay has proven to be suitable for studying complex degradation processes involving various immunoglobulin G1 (IgG1) molecules. Assignment of covalent degradations to specific regions of mAbs was facilitated by using Lys-C and papain to generate Fab and Fc fragments with unique, protease-dependent elution times. In particular, this method was useful for characterizing protein variants formed in the presence of salt under accelerated storage conditions. Two isoforms that accumulated during storage were readily identified as Fab-related species prior to mass-spectrometric analysis. Both showed reduced biological activity likely resulting from modifications within or in proximity of the complementarity-determining regions (CDRs). Utility of this assay was further illustrated in the work to characterize light-induced degradations in mAb formulations. In this case, a previously unknown Fab-related species which populated upon light exposure was observed. This species was well resolved from unmodified Fab, allowing for direct and high-purity fractionation. Mass-spectrometric analysis subsequently identified a histidine-related degradation product associated with the CDR2 of the heavy chain. In addition, the method was applied to assess the structural organization of a noncovalent IgG1 dimer. A new species corresponding to a Fab–Fab complex was found, implying that interactions between Fab domains were responsible for dimerization. Overall, the data presented demonstrate the suitability of this cation-exchange HPLC method for studying a wide range of covalent and noncovalent degradations in IgG1 mAbs.     

Non-covalent interactions between Fab and Fc regions in immunoglobulin G molecules. Hydrogen-deuterium exchange studies

To reveal non-covalent interactions between the Fab and Fc regions of IgG molecules the average conformational free-energy change (delta Go), associated with reversible micro-unfoldings, was measured by hydrogen-deuterium exchange for the Fab and Fc fragments and the complete molecule. Human monoclonal IgG1 and pooled IgG samples were used in these experiments. Hydrogen-deuterium exchange data were summarized and compared in the form of exchange relaxation spectra. The experimentally observed relaxation spectrum of intact IgG could not be deduced by weighted summation of spectra measured for Fab and Fc fragments. A comparison of the measured and calculated data revealed a 5-kJ/mol increase in the conformational free energy upon splitting the IgG molecule into two Fab and Fc pieces, i.e. an increase of conformational mobility occurred. This change can be explained either by related fluctuation patterns of the Fab and Fc pieces in the intact molecule or by a shielding effect on the contact surfaces. Both interpretations suppose non-covalent interactions between Fab and Fc that can be a means of information transduction between recognition and effector sites. The pH dependence of the hydrogen-deuterium exchange also indicates interactions between the Fab and Fc regions. A shift in the relaxation spectra of the Fab fragment was observed between pH 8.2 and 7.3 revealing destabilization of the structure at lower pH. This effect is absent in the intact molecule, reflecting interactions that stabilize the Fab structure. Comparison of the relaxation spectra of Fab and Fc shows a difference of about 10 kJ/mol in the microstability of these fragments: the Fab part possesses more conformational flexibility (i.e. its microstability is smaller) than the Fc part.     

Charge-mediated Fab-Fc interactions in an IgG1 antibody induce reversible self-association,cluster formation,and elevated viscosity

Concentration-dependent reversible self-association (RSA) of monoclonal antibodies (mAbs) poses a challenge to their pharmaceutical development as viable candidates for subcutaneous delivery. While the role of the antigen-binding fragment (Fab) in initiating RSA is well-established, little evidence supports the involvement of the crystallizable fragment (Fc). In this report, a variety of biophysical tools, including hydrogen exchange mass spectrometry, are used to elucidate the protein interface of such non-covalent protein-protein interactions. Using dynamic and static light scattering combined with viscosity measurements, we find that an IgG1 mAb (mAb-J) undergoes RSA primarily through electrostatic interactions and forms a monomer-dimer-tetramer equilibrium. We provide the first direct experimental mapping of the interface formed between the Fab and Fc domains of an antibody at high protein concentrations. Charge distribution heterogeneity between the positively charged interface spanning complementarity-determining regions CDR3H and CDR2L in the Fab and a negatively charged region in C_H3/Fc domain mediates the RSA of mAb-J. When arginine and NaCl are added, they disrupt RSA of mAb-J and decrease the solution viscosity. Fab-Fc domain interactions between mAb monomers may promote the formation of large transient antibody complexes that ultimately cause increases in solution viscosity. Our findings illustrate how limited specific arrangements of amino-acid residues can cause mAbs to undergo RSA at high protein concentrations and how conserved regions in the Fc portion of the antibody can also play an important role in initiating weak and transient protein-protein interactions.     

Protein aggregation and mitigation strategy in low pH viral inactivation for monoclonal antibody purification

ABSTRACT

Significant amounts of soluble product aggregates were observed during low-pH viral inactivation (VI) scale-up for an IgG4 monoclonal antibody (mAb IgG4-N1), while small-scale experiments in the same condition showed negligible aggregation. Poor mixing and product exposure to low pH were identified as the root cause. To gain a mechanistic understanding of the problem, protein aggregation properties were studied by varying critical parameters including pH, hold time and protein concentration. Comprehensive biophysical characterization of product monomers and aggregates was performed using fluorescence-size-exclusion chromatography, differential scanning fluorimetry, fluorescence spectroscopy, and dynamic light scattering. Results showed IgG4-N1 partially unfolds at about pH 3.3 where the product molecules still exist largely as monomers owing to strong inter-molecular repulsions and favorable colloidal stability. In the subsequent neutralization step, however, the conformationally changed monomers are prone to aggregation due to weaker inter-molecular repulsions following the pH transition from 3.3 to 5.5. Surface charge calculations using homology modeling suggested that intra-molecular repulsions, especially between CH2 domains, may contribute to the IgG4-N1 unfolding at ≤ pH 3.3. Computational fluid dynamics (CFD) modeling was employed to simulate the conditions of pH titration to reduce the risk of aggregate formation. The low-pH zones during acid addition were characterized using CFD modeling and correlated to the condition causing severe product aggregation. The CFD tool integrated with the mAb solution properties was used to optimize the VI operating parameters for successful scale-up demonstration. Our research revealed the governing aggregation mechanism for IgG4-N1 under acidic conditions by linking its molecular properties and various process-related parameters to macroscopic aggregation phenomena. This study also provides useful insights into the cause and mitigation of low-pH-induced IgG4 aggregation in downstream VI operation.     

Fractionation of IgG fragments using reversed micellar extraction

Reversed micellar extraction was applied for the fractionation of IgG fragments. With isooctane solution containing 50 mM AOT, Fab, Fe and IgG were extracted to the micellar phase. Each protein had an optimum pH range in the extraction. Fab and Fc were separated from the mixture at pH 7.0, with Fab being extracted to the micellar phase and Fe remaining in the aqueous phase. Extracted Fab fragments were recovered by bringing them into contact with 6M guanidine/HCl followed by dilution with PBS. Fab and Fc fragments were separated and recovered by reversed micellar extraction from IgG lysate digested with papain. Since the procedure is simple and rapid compared with column chromatography, mass preparation of the fragments can be expected by this method.     

抗甲肝病毒基因工程单抗分离纯化与鉴定

为克服血源免疫球蛋白制品的不足,开发了抗甲肝病毒基因工程单克隆抗体anti-HAV IgG。用无血清培养基培养rCHO工程细胞株,上清液经过rProtein A SFF亲和层析→脱盐→离子交换层析→超滤换液纯化后,所得anti-HAV IgG纯度达99%以上,比活性约100IU/mg,anti-HAV IgG活性回收率40%。所纯化的anti-HAV IgG分子量150kD,等电点8.4～9.3。免疫印迹实验证实anti-HAV IgG为人源全抗体分子。亲和层析介质rProtein A SFF确实存在亲和配基脱落问题,但通过后续纯化步骤可有效除去。在亲和层析过程中加入高盐清洗步骤,可有效降低宿主DNA残留量水平。对样品中自由巯基含量进行了测定,认为非还原电泳图谱中低分子量条带是由于抗体分子内存在自由巯基引起。用该工艺制备的anti-HAV IgG各项纯度检测指标均达到我国对基因工程产品的质量要求。     

A novel method for continuous chromatographic separation of monoclonal antibody charge variants by combining displacement mode chromatography and step elution

Charge heterogeneity of monoclonal antibodies is considered a critical quality attribute and hence needs to be monitored and controlled by the manufacturer. Typically, this is accomplished via separation of charge variants on cation exchange chromatography (CEX) using a pH or conductivity based linear gradient elution. Although an effective approach, this is challenging particularly during continuous processing as creation of linear gradient during continuous processing adds to process complexity and can lead to deviations in product quality upon slightest changes in gradient formation. Moreover, the long length of elution gradient along with the required peak fractionation makes process integration difficult. In this study, we propose a novel approach for separation of charge variants during continuous CEX chromatography by utilizing a combination of displacement mode chromatography and salt-based step elution. It has been demonstrated that while the displacement mode of chromatography enables control of acidic variants ≤26% in the CEX eluate, salt-based step gradient elution manages basic charge variant ≤25% in the CEX eluate. The proposed approach has been successfully demonstrated using feed materials with varying compositions. On comparing the designed strategy with 2-column concurrent (CC) chromatography, the resin specific productivity increased by 95% and resin utilization increased by 183% with recovery of main species >99%. Further, in order to showcase the amenability of the designed CEX method in continuous operation, the method was examined in our in-house continuous mAb platform.     

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.     

Rates and impact of human antibody glycation in vivo

Glycation of immunoglobulin G (IgG) can result from incubation with a reducing sugar in vitro or during circulation in vivo. Upon injection of a recombinantly produced human therapeutic IgG into humans, changes in the glycation levels could be observed as a function of circulation time. Mass changes on the individual IgG polypeptide chains as the results of glycation were determined using reversed-phase liquid chromatography/mass spectrometry. Changes to the light and heavy chains were low but easily detectable at 0.00092 and 0.0021 glucose (Glc) additions per chain per day, respectively. Levels of glycation found on the Fc portion of IgG isolated from healthy subjects, using a similar analytical approach, were on average 0.045 Glc molecules per fragment. In vivo glycation rates could be approximated in vitro by modeling the physiological glycation reaction with a simplified incubation containing physiological Glc concentrations, pH and temperature but with a high concentration of a single purified IgG. To test the impact of glycation on IgG function, highly glycated IgG1 and IgG2 were prepared containing on average 42-49 Glc molecules per IgG. Binding to FcγIIIa receptors, neonatal Fc receptor or protein A was similar or identical to the non-glycated IgG controls. Although the modifications were well distributed throughout the protein sequence, and at high enough levels to affect the elution position by size-exclusion chromatography, no changes in the tested Fc functions were observed.     

Analysis of human antibody IgG2 domains by reversed-phase liquid chromatography and mass spectrometry

It has been well documented that papain cleaves an IgG1 molecule to release Fab and Fc domains; however, papain was found unable to release such domains from an IgG2. Here we present a new combinatory strategy to analyze the heterogeneity of the light chain (LC), single chain Fc (sFc), and Fab portion of the heavy chain (Fd) of an IgG2 molecule released by papain cleavage under mild reducing conditions. These domains were well separated on reversed-phase high performance liquid chromatography (RP-HPLC) and analyzed by in-line liquid chromatography time-of-flight mass spectrometry (LC–TOF/MS). In addition, some modifications of these domains were revealed by in-line mass spectrometry, and confirmed by the peptide mapping on LC–MS/MS analysis. This same strategy was proven suitable for IgG1 molecules as well. This procedure provides a simplified approach for the characterization of antibody biomolecules by facilitating the detection of low-level modifications in a domain. In addition, the technique offers a new strategy as an identification assay to distinguish IgG2 molecules on RP-HPLC, by which highly conserved Fc domains remain at a constant retention time (RT) unique to its subisotype, while varying RTs of the light chain and the Fd distinguish the monoclonal antibody from other molecules of the same isotype based on the underlying characteristics of each antibody.     

Analytical FcRn affinity chromatography for functional characterization of monoclonal antibodies

The neonatal Fc receptor (FcRn) is important for the metabolic fate of IgG antibodies in vivo. Analysis of the interaction between FcRn and IgG in vitro might provide insight into the structural and functional integrity of therapeutic IgG that may affect pharmacokinetics (PK) in vivo. We developed a standardized pH gradient FcRn affinity liquid chromatography method with conditions closely resembling the physiological mechanism of interaction between IgG and FcRn. This method allows the separation of molecular IgG isoforms, degradation products and engineered molecules based on their affinity to FcRn. Human FcRn was immobilized on the column and a linear pH gradient from pH 5.5 to 8.8 was applied. FcRn chromatography was used in comparison to surface plasmon resonance to characterize different monoclonal IgG preparations, e.g., oxidized or aggregated species. Wild-type and engineered IgGs were compared in vitro by FcRn chromatography and in vivo by PK studies in huFcRn transgenic mice. Analytical FcRn chromatography allows differentiation of IgG samples and variants by peak pattern and retention time profile. The method can distinguish: 1) IgGs with different Fabs, 2) oxidized from native IgG, 3) aggregates from monomer and 4) antibodies with mutations in the Fc part from wild-type IgGs. Changes in the FcRn chromatographic behavior of mutant IgGs relative to the wild-type IgG correlate to changes in the PK profile in the FcRn transgenic mice. These results demonstrate that FcRn affinity chromatography is a useful new method for the assessment of IgG integrity.     

Influence of N-glycosylation on effector functions and thermal stability of glycoengineered IgG1 monoclonal antibody with homogeneous glycoforms

Glycosylation of the conserved asparagine residue in each heavy chain of IgG in the CH2 domain is known as N-glycosylation. It is one of the most common post-translational modifications and important critical quality attributes of monoclonal antibody (mAb) therapeutics. Various studies have demonstrated the effects of the Fc N-glycosylation on safety, Fc effector functions, and pharmacokinetics, both dependent and independent of neonatal Fc receptor (FcRn) pathway. However, separation of various glycoforms to investigate the biological and functional relevance of glycosylation is a major challenge, and existing studies often discuss the overall impact of N-glycans, without considering the individual contributions of each glycoform when evaluating mAbs with highly heterogeneous distributions. In this study, chemoenzymatic glycoengineering incorporating an endo-β-N-acetylglucosaminidase (ENGase) EndoS2 and its mutant with transglycosylation activity was used to generate mAb glycoforms with highly homogeneous and well-defined N-glycans to better understand and precisely evaluate the effect of each N-glycan structure on Fc effector functions and protein stability. We demonstrated that the core fucosylation, non-reducing terminal galactosylation, sialylation, and mannosylation of IgG1 mAb N-glycans impact not only on FcγRIIIa binding, antibody-dependent cell-mediated cytotoxicity, and C1q binding, but also FcRn binding, thermal stability and propensity for protein aggregation.     

Optimizing the Performance of Chromatographic Separations Using Microfluidics: Multiplexed and Quantitative Screening of Ligands and Target Molecules

The optimization of chromatography ligands for the purification of biopharmaceuticals is highly demanded to meet the needs of the pharmaceutical industry. In the case of monoclonal antibodies (mAbs), synthetic ligands comprising multiple types of interactions (multimodal) provide process and economic advantages compared to protein‐based affinity ligands. However, optimizing the operation window of these ligands requires the development of effective high‐throughput screening platforms. Here, a novel microfluidics‐based methodology to perform rapid and multiplexed screening of various multimodal ligands relative to their ability to bind different target molecules is demonstrated. The microfluidic structure comprises three individual chambers (≈8 nL each) packed with different types of chromatography beads in series with the feed flow. An artificial mixture composed of immunoglobulin G (IgG) and bovine serum albumin, labeled with different thiol‐reactive neutral fluorescent dyes, is used as a model to quantitatively optimize the performance (yield and purity) of the separation. This approach can potentially be used as a predictive analytical tool in the context of mAb purification, allowing low consumption of molecules and providing results in <3 min. Furthermore, this versatile approach can potentially be extended not only with respect to the number of different resins and target molecules, but also for parallel analysis of multiple conditions.     

Impact of deglycosylation and thermal stress on conformational stability of a full length murine igG2a monoclonal antibody: Observations from molecular dynamics simulations

With the rise of antibody based therapeutics as successful medicines, there is an emerging need to understand the fundamental antibody conformational dynamics and its implications towards stability of these medicines. Both deglycosylation and thermal stress have been shown to cause conformational destabilization and aggregation in monoclonal antibodies. Here, we study instabilities caused by deglycosylation and by elevated temperature (400 K) by performing molecular dynamic simulations on a full length murine IgG2a mAb whose crystal structure is available in the Protein Data bank. C^α‐atom root mean square deviation and backbone root mean square fluctuation calculations show that deglycosylation perturbs quaternary and tertiary structures in the C_H2 domains. In contrast, thermal stress pervades throughout the antibody structure and both Fabs and Fc regions are destabilized. The thermal stress applied in this study was not sufficient to cause large scale unfolding within the simulation time and most amino acid residues showed similar average solvent accessible surface area and secondary structural conformations in all trajectories. C_H3 domains were the most successful at resisting the conformational destabilization. The simulations helped identify aggregation prone regions, which may initiate cross‐β motif formation upon deglycosylation and upon applying thermal stress. Deglycosylation leads to increased backbone fluctuations and solvent exposure of a highly conserved APR located in the edge β‐strand A of the C_H2 domains. Aggregation upon thermal stress is most likely initiated by two APRs that overlap with the complementarity determining regions. This study has important implications for rational design of antibody based therapeutics that are resistant towards aggregation. Proteins 2013. © 2012 Wiley Periodicals, Inc.     

Solution structures of human myeloma IgG3 antibody reveal extended Fab and Fc regions relative to the other IgG subclasses

Human immunoglobulin G subclass 3 (IgG3) possesses a uniquely long hinge region that separates its Fab antigen-binding and Fc receptor-binding regions. Owing to this hinge length, the molecular structure of full-length IgG3 remains elusive, and the role of the two conserved Fc glycosylation sites are unknown. To address these issues, we subjected glycosylated and deglycosylated human myeloma IgG3 to multidisciplinary solution structure studies. Using analytical ultracentrifugation, the elongated structure of IgG3 was determined from the reduced sedimentation coefficients s⁰_20,w of 5.82 to 6.29 S for both glycosylated and deglycosylated IgG3. X-ray and neutron scattering showed that the Guinier R_G values were 6.95 nm for glycosylated IgG3 and were unchanged after deglycosylation, again indicating an elongated structure. The distance distribution function P(r) showed a maximum length of 25 to 28 nm and three distinct maxima. The molecular structure of IgG3 was determined using atomistic modeling based on molecular dynamics simulations of the IgG3 hinge and Monte Carlo simulations to identify physically realistic arrangements of the Fab and Fc regions. This resulted in libraries containing 135,135 and 73,905 glycosylated and deglycosylated IgG3 structures, respectively. Comparisons with the X-ray and neutron scattering curves gave 100 best-fit models for each form of IgG3 that accounted for the experimental scattering curves. These models revealed the first molecular structures for full-length IgG3. The structures exhibited relatively restricted Fab and Fc conformations joined by an extended semirigid hinge, which explains the potent effector functions of IgG3 relative to the other subclasses IgG1, IgG2, and IgG4.