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

Abstract 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.