Identification of a CE-SDS shoulder peak as disulfide-linked fragments from common CH2 cleavages in IgGs and IgG-like bispecific antibodies

Effects of process intensification on homogeneity of an IgG1:κ monoclonal antibody during perfusion culture

The pharmaceutical industry employs various strategies to improve cell productivity. These strategies include process intensification, culture media improvement, clonal selection, media supplementation and genetic engineering of cells. However, improved cell productivity has inherent risk of impacting product quality attributes (PQA). PQAs may affect the products' efficacy via stability, bioavailability, or in vivo bioactivity. Variations in manufacturing process may introduce heterogeneity in the products by altering the type and extent of N-glycosylation, which is a PQA of therapeutic proteins. We investigated the effect of different cell densities representing increasing process intensification in a perfusion cell culture on the production of an IgG1-κ monoclonal antibody from a CHO-K1 cell line. This antibody is glycosylated both on light chain and heavy chain. Our results showed that the contents of glycosylation of IgG1-κ mAb increased in G0F and fucosylated type glycans as a group, whereas sialylated type glycans decreased, for the mAb whole protein. Overall, significant differences were observed in amounts of G0F, G1F, G0, G2FS1, and G2FS2 type glycans across all process intensification levels. G2FS2 and G2 type N-glycans were predominantly quantifiable from light chain rather than heavy chain. It may be concluded that there is a potential impact to product quality attributes of therapeutic proteins during process intensification via perfusion cell culture that needs to be assessed. Since during perfusion cell culture the product is collected throughout the duration of the process, lot allocation needs careful attention to process parameters, as PQAs are affected by the critical process parameters (CPPs). KEY POINTS: • Molecular integrity may suffer with increasing process intensity. • Galactosylated and sialylated N-glycans may decrease. • Perfusion culture appears to maintain protein charge structure.

Characterization of mAb size heterogeneity originating from a cysteine to tyrosine substitution using denaturing and native LC-MS

Upon assessing the comparability between a biosimilar mAb and its reference product by non-reducing CE-SDS, increased levels of a heavy-heavy-light chain (HHL) variant, present as a low molecular weight (LMW) peak, were observed. RPLC-MS applied at top, middle-up and bottom-up level revealed the existence of Cys-to-Tyr substitutions, predominantly at position HC226 involved in connecting LC and HC, explaining the abundant HHL levels. Antigen binding was not impacted by the presence of this size variant suggesting a non-covalent association of Tyr substituted HHL and LC. The latter complex is not maintained in the denaturing conditions associated with CE-SDS and RPLC-MS. Its existence could, nevertheless, be confirmed by native SEC-MS which preserves non-covalent protein interactions during separation and electrospray ionization. Amino acid analysis furthermore demonstrated a depletion of Cys during the fed-batch process indicating that the observed size/sequence variant is not of genetic but rather of metabolic origin. Native SEC-MS showed that supplementing the cell culture medium with Cys halts misincorporation of Tyr and promotes the formation of the desired mAb structure. To the best of our knowledge, Cys-to-Tyr substitutions preventing interchain disulfide bridge formation have not been described earlier. This observation adds to the impressive structural heterogeneity reported to date for mAbs.

Monoclonal Antibody Sequence Variants Disguised as Fragments: Identification, Characterization, and Their Removal by Purification Process Optimization

During early stage development of a therapeutic IgG1 monoclonal antibody, high levels of low molecular weight (LMW) peaks were observed by high performance size-exclusion chromatography and capillary electrophoresis. Further characterization of the LMW peak enriched HPSEC fractions using reversed phase liquid chromatography coupled to mass spectrometry showed these LMW species were 47 kDa and 50 kDa in size. However, the measured masses could not be matched to any fragments resulting from peptide bond hydrolysis. To identify these unknown LMW species, molecular characterization methods were employed, including high-throughput sequencing of RNA. Transcriptomic analysis revealed the LMW species were generated by mis-splicing events in the heavy chain transcript, which produced truncated heavy chain products that assembled with the light chain to mimic the appearance of fragments identified by routine purity assays. In an effort to improve product quality, an optimized purification process was developed. Characterization of the process intermediates confirmed removal of both LMW species by the optimized process. Our study demonstrates that deep-dive analytical characterization of biotherapeutics is critical to ensure product quality and inform process development. Transcriptomic analysis tools can help identify the cause of unknown species, and plays a key role in product and process characterization.