Conversion of a CHO cell culture process from perfusion to fed-batch technology without altering product quality.
During the development of a new drug product, it is a common strategy to develop a first-generation process with the aim to rapidly produce material for pre-clinical and early stage clinical trials. At a later stage of the development, a second-generation process is then introduced with the aim to supply late-stage clinical trials as well as market needs. This work was aimed at comparing the performance of two different CHO cell culture processes (perfusion and fed-batch) used for the production of a therapeutically active recombinant glycoprotein at industrial pilot-scale. The first-generation process was based on the Fibra-Cel packed-bed perfusion technology. It appeared during the development of the candidate drug that high therapeutic doses were required (>100mg per dose), and that future market demand would exceed 100 kg per year. This exceeded by far the production capacity of the first-generation process, and triggered a change of technology from a packed-bed perfusion process with limited scale-up capabilities to a fed-batch process with scale-up potential to typical bioreactor sizes of 15m(3) or more. The productivity per bioreactor unit volume (in product m(-3)year(-1)) of the fed-batch process was about 70% of the level reached with the first-generation perfusion process. However, since the packed-bed perfusion system was limited in scale (0.6m(3) maximum) compared to the volumes reached in suspension cultures (15m(3)), the fed-batch was selected as second-generation process. In fact, the overall process performance (in product year(-1)) was about 18-fold higher for the fed-batch compared to the perfusion mode. Data from perfusion and fed-batch harvests samples indicated that comparable product quality (relative abundance of monomers dimers and aggregates; N-glycan sialylation level; isoforms distribution) was obtained in both processes. To further confirm this observation, purification to homogeneity of the harvest material from both processes, followed by a complementary set of studies (e.g. full physico-chemical characterization, assessment of in vitro and in vivo bioactivity, comparative pharmacokinetics and pharmacodynamics studies in relevant species, etc.) would be required. Finally, this illustrates the need to fix the production process early during the development of a new drug product in order to minimize process conversion efforts and to shorten product development time lines.
Meuwly
F
F
Serono Biotech Center, Laboratoires Serono S.A., Zone Industrielle B, CH-1809 Fenil-sur-Corsier, Switzerland.
Weber
U
U
Ziegler
T
T
Gervais
A
A
Mastrangeli
R
R
Crisci
C
C
Rossi
M
M
Bernard
A
A
von Stockar
U
U
Kadouri
A
A
D000818:Animals; D019149:Bioreactors; D001709:Biotechnology / Q000295:instrumentation / Q000379:methods; D016466:CHO Cells / Q000502:physiology*; D018929:Cell Culture Techniques / Q000295:instrumentation* / Q000379:methods*; D049109:Cell Proliferation; D003198:Computer Simulation; D017076:Computer-Aided Design; D006224:Cricetinae; D003412:Cricetulus; D004867:Equipment Design; D019544:Equipment Failure Analysis; D008954:Models, Biological; D010477:Perfusion; D011786:Quality Control; D011994:Recombinant Proteins / Q000096:biosynthesis*
D011994:Recombinant Proteins