Considerations for operational space definition and optimization of a no-salt flowthrough hydrophobic interaction chromatography purification step.

No-salt flowthrough hydrophobic interaction chromatography (HIC) has been shown to effectively remove process and product-related impurities from bioprocess streams. In this publication, a panel of six antibodies has been used to demonstrate operating principles for the application of no-salt flowthrough HIC in antibody purification processes. The results indicate that no-salt flowthrough HIC provides robust aggregate clearance across operating conditions including flow rate, and variations in resin ligand density. Additionally, HMW reduction has an optimal pH range relative to the isoelectric point of each molecule and high molecular weight (HMW) reduction can be improved by altering the total protein load and/or HMW concentration to drive binding of high molecular weight species to the resin.

Twenty plus Years of Data Demonstrating Virus Filtration as an Effective and Robust Step for Large Virus Removal.

Virus filtration has been demonstrated to be an effective and robust dedicated viral clearance step that is used in biopharmaceutical manufacturing processes. Here we present virus filtration data from a multicompany collaboration with data compiled from WuXi Advanced Therapies' and Charles River Laboratories' internal viral clearance databases spanning more than 25 years. The data were sorted by virus removal and type and then further subdivided into murine leukemia virus only, pseudorabies virus only, and reovirus type 3 only categories to allow for analyses of viral clearance results. A total of 2311 virus filtrations were analyzed, composed of 1516 murine leukemia virus, 385 pseudorabies virus, and 410 reovirus type 3 virus filtrations. These data provide clear evidence that will help supplement both internal and industry-wide initiatives focused on using prior knowledge for the creation of modular claims for small virus retentive filters and allow better allocations of resources typically spent on potentially unnecessary studies.

Discovery and Characterization of Histidine Oxidation Initiated Cross-links in an IgG1 Monoclonal Antibody.

Novel cross-links between an oxidized histidine and intact histidine, lysine, or cysteine residues were discovered and characterized from high-molecular weight (HMW) fractions of an IgG1 monoclonal antibody (mAb). The mAb HMW fractions were collected using preparative size-exclusion chromatography (SEC) and extensively characterized to understand the mechanism of formation of the nonreducible and covalently linked portion of the HMWs. The HMW fractions were IdeS digested, reduced, and analyzed by size-exclusion chromatography coupled with mass spectrometry (SEC-MS). The nonreducible cross-links were found to be enriched in the fragment crystallizable (Fc) region of the heavy chain, with a net mass increase of 14 Da. Detailed peptide mapping revealed as many as seven covalent cross-links in the HMW fractions, where oxidized histidines react with intact histidine, lysine, and free cysteine to form cross-links. It is the first time that histidine-cysteine (His-Cys) and histidine-lysine (His-Lys) in addition to histidine-histidine (His-His) cross-links were discovered in monoclonal antibody HMW species. The histidine oxidation hot spots were identified, which include conserved histidine residues His292 and His440 in the Fc region and His231 in the hinge region of the IgG1 mAb heavy chain. Their cross-linking partners include His231, His292, His440, and Cys233 in the hinge region and Lys297 in the Fc region. A cross-linking mechanism has been proposed that involves nucleophilic addition by histidine, cysteine, or lysine residues to the carbonyl-containing histidine oxidation intermediates to form the cross-links.