A purification process scheme was developed to purify therapeutic-grade human monoclonal antibodies. It features two columns with interchangeable chromatography steps and non-affinity resins. The purification scheme includes a cation exchange column (CEX) and a hydrophobic charge induction (HCI) column and eliminates the need of an in-process diafiltration step. Viral clearance from this scheme is efficient due to the ability of HCI resin to remove adventitious agents. The scheme was scaled up 1,000- to 10,000-fold with an average overall yield >70% for a variety of antibodies. Contaminant removal and product quality from this process are comparable to those of three-column affinity and non-affinity purification schemes.
Affinity chromatography often is used as a capture step to meet purity, yield, and throughput requirements, despite the development of advanced chromatography resins with improved performance at high flow rates and binding capacity. Traditionally, the affinity-based capture step (Protein A or G) is followed by at least one or two other chromatography steps. In addition, one or more in-process diafiltration steps are needed to condition the feed into the following column. Not only is Protein A resin at least four to five times more expensive than non-affinity media, it can also have issues such as ligand leaching. In general, even if affinity chromatography is used, adequate purity and viral clearance often are not achieved unless one or more polishing steps are interspersed.
By eliminating specific steps in downstream processing, productivity can be maximized while maintaining the integrity and purity of the molecule. We describe here a flexible, interchangeable, non-affinity, two-step purification method that can be implemented at lower cost compared to affinity-based schemes due to its simplicity and short number of steps involved. Overall recovery is high and final product quality is equivalent to more traditional protocols.
Not only did we reduce the number of steps with the proposed purification process, but we also eliminate the need for an in-process concentration or diafiltration (which would mean more development, optimization, scale-up, cleaning and cleaning validation, and increased process cost while risking potential loss or modification of product). Minimizing the number of steps will cut down the number of process components, buffers, tanks, and miscellaneous equipment. Finally, the two-column purification process can be readily implemented into the clinical manufacturing of many antibody molecules with less initial investment on development cost, time, and resource requirements.
TWO-COLUMN PURIFICATION PROCESS
This purification process explores the integration of the separation principles of two different resins, a cation exchange (CEX) resin (Poros 50HS or Fractogel EMD SE HiCap) and a hydrophobic charge induction (HCI) resin (MEP HyperCel). The proposed scheme adapts to different feed types and user implementation choices, while still clearing host cell proteins (HCPs), viral-like particles, nucleic acids, product-related contaminants, and media additives (e.g., methatrexate, insulin, vitamins) to levels that allow the therapeutic use of the final purified material.