TY - JOUR
T1 - Integrated double flow-through purification of monoclonal antibodies using membrane adsorbers and single-pass tangential flow filtration
AU - Schmitz, Fabian
AU - Kruse, Thomas
AU - Minceva, Mirjana
AU - Kampmann, Markus
N1 - Publisher Copyright:
© 2023 The Authors
PY - 2023/6
Y1 - 2023/6
N2 - A flow-through process for monoclonal antibody (mAb) purification has been created by integrating two different membrane adsorbers (MAs) with single-pass tangential flow filtration (SPTFF) for continuous buffer exchange. First, a design of experiments (DoE) was carried out to investigate the influence of pH and conductivity on the removal of desoxyribonucleic acid (DNA) and host cell proteins (HCP), and to select buffer conditions for mAb flow-through mode operation for four different MAs. As next, breakthrough curve experiments were performed with the selected buffer conditions for each MA to analyze the binding behavior of mAb, DNA, and HCP. Then, the influence of the MA sequence in the double flow-through process on the mAb yield and DNA and HCP removal was studied in batch mode. The best sequence of MAs was used for the final integrated double flow-through polishing process, where the MAs were directly connected via SPTFF. The flow-through of the first (anion exchange) MA was continuously diafiltrated via SPTFF to buffer conditions for the second (cation exchange) MA. In this way, DNA (< 2 ppm) and HCP (< 29 ppm) were removed with simultaneously high mAb yield. Moreover, 36 times higher throughput was obtained than with a standard process that combines a packed-bed column with CEX resin in a bind and elute mode with an AEX MA in flow-through mode.
AB - A flow-through process for monoclonal antibody (mAb) purification has been created by integrating two different membrane adsorbers (MAs) with single-pass tangential flow filtration (SPTFF) for continuous buffer exchange. First, a design of experiments (DoE) was carried out to investigate the influence of pH and conductivity on the removal of desoxyribonucleic acid (DNA) and host cell proteins (HCP), and to select buffer conditions for mAb flow-through mode operation for four different MAs. As next, breakthrough curve experiments were performed with the selected buffer conditions for each MA to analyze the binding behavior of mAb, DNA, and HCP. Then, the influence of the MA sequence in the double flow-through process on the mAb yield and DNA and HCP removal was studied in batch mode. The best sequence of MAs was used for the final integrated double flow-through polishing process, where the MAs were directly connected via SPTFF. The flow-through of the first (anion exchange) MA was continuously diafiltrated via SPTFF to buffer conditions for the second (cation exchange) MA. In this way, DNA (< 2 ppm) and HCP (< 29 ppm) were removed with simultaneously high mAb yield. Moreover, 36 times higher throughput was obtained than with a standard process that combines a packed-bed column with CEX resin in a bind and elute mode with an AEX MA in flow-through mode.
KW - Flow-through chromatography
KW - Integrated process
KW - Monoclonal antibody purification
KW - Process intensification
KW - Single-pass tangential flow filtration
UR - http://www.scopus.com/inward/record.url?scp=85151262088&partnerID=8YFLogxK
U2 - 10.1016/j.bej.2023.108913
DO - 10.1016/j.bej.2023.108913
M3 - Article
AN - SCOPUS:85151262088
SN - 1369-703X
VL - 195
JO - Biochemical Engineering Journal
JF - Biochemical Engineering Journal
M1 - 108913
ER -