Abstract

The goal of cell culture process intensification is to increase volumetric productivity, generally by increasing viable cell density (VCD), cell specific productivity or production bioreactor utilization in manufacturing. In our previous study, process intensification in fed-batch production with higher titer or shorter duration was demonstrated by increasing the inoculation seeding density (SD) from ~ 0.6 (Process A) to 3–6 × 106 cells/mL (Process B) in combination with media enrichment. In this study, we further increased SD to 10–20 × 106 cells/mL (Process C) using perfusion N-1 seed cultures, which increased titers already at industrially relevant levels by 100% in 10–14 day bioreactor durations for four different mAb-expressing CHO cell lines. Redesigned basal and feed media were critical for maintaining higher VCD and cell specific productivity during the entire production duration, while medium enrichment, feeding strategies and temperature shift optimization to accommodate high VCDs were also important. The intensified Process C was successfully scaled up in 500-L bioreactors for 3 of the 4 mAbs, and quality attributes were similar to the corresponding Process A or Process B at 1000-L scale. The fed-batch process intensification strategies developed in this study could be applied for manufacturing of other mAbs using CHO and other host cells.

Details

Title
Development of an intensified fed-batch production platform with doubled titers using N-1 perfusion seed for cell culture manufacturing
Author
Xu, Jianlin 1 ; Rehmann, Matthew S 1 ; Xu Mengmeng 1 ; Zheng Shun 1 ; Hill, Charles 1 ; He, Qin 1 ; Borys, Michael C 1 ; Li, Zheng Jian 1 

 Bristol-Myers Squibb Company, Global Product Development and Supply, Devens, USA (GRID:grid.419971.3) 
Publication year
2020
Publication date
Dec 2020
Publisher
Springer Nature B.V.
e-ISSN
21974365
Source type
Scholarly Journal
Language of publication
English
ProQuest document ID
2381954506
Copyright
Bioresources and Bioprocessing is a copyright of Springer, (2020). All Rights Reserved. This work is published under http://creativecommons.org/licenses/by/4.0/ (the “License”). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.