Performance comparison of protein A affinity resins for the purification of monoclonal antibodies.

During the selection of protein A affinity resin for the purification of monoclonal antibodies, dynamic binding capacity (Q(dyn10%)), volumetric production rate (Pr(vol)) and 'process robustness' are essential parameters to be evaluated. In this article, empirical mathematical models describe these parameters as a function of antibody concentration in load (C0), load flow rate (u(load)) and bed height (L). These models allow us to select optimal process conditions for each of the evaluated protein A affinity resins. C0, u(load) and L largely affect dynamic binding capacity (Q(dyn10%)) and volumetric production rate (Pr(vol)). Maximum Q(dyn10%) is generally obtained at high C0 and at low u(load). Maximum Pr(vol) is obtained at high C0 and at lowest L, run at high u(load). All evaluated resins have a relatively high robustness against variations in C0. |DeltaQ(dyn10%)/deltaC0| ranges from 0.0 to 7.8. It is clear that Q(dyn10%), Pr(vol) and 'process robustness' cannot be maximized all at the same time. Furthermore, some other aspects like IgG recovery, protein A leaching, easiness to pack, easiness to clean, number of re-uses and cost of production might be important to be taken into the equation. Certain evaluation parameters may be more important than others, depending on the specific situation. Therefore, a case-by-case evaluation is recommended.

A potential generic downstream process using Cibracon Blue resin at very high loading capacity produces a highly purified monoclonal antibody preparation from cell culture harvest.

The use of a dye-ligand chromatography for the purification of monoclonal antibody (MAb) from cell culture and other feed streams has been largely overlooked in large scale production. Cibracon Blue dye (CB), a polycyclic anionic ligand, interacts with protein through a specific interaction between the dye, acting as a mimic of NAD+ and NADP+, or through non-specific electrostatic, hydrophobic, and other forces. In this paper, a CB resin was used to effectively and efficiently separate an IgG4 MAb from host and process impurities following the capture of the MAb on a Protein-A (PA) column. The CB unit operation, challenged at 99% by reducing SDS-PAGE). A facile three column scalable production scheme, employing CB as the second column in the process was used to generate highly purified MAb from cell culture harvest derived from two media of very different compositions. Free CB dye was