Related Experiment Video
Updated: Jul 3, 2026

Cultivation of Mammalian Cells Using a Single-use Pneumatic Bioreactor System
Published on: October 10, 2014
A fiber-bed bioreactor for anchorage-dependent animal cell cultures: part II. Scaleup potential
S Murakami1, T W Chiou, D I Wang
1Biotechnology Process Engineering Center, Massachusetts Institute of Technology, Cambridge, Massachusetts 02139, USA.
Abstract:
A simple hydrodynamic model is introduced to describe the airlift fiber-bed bioreactor, which can enhance the volumetric productivity of anchorage-dependent animal cell cultures. By applying the model, liquid flow rates and volumetric mass transfer coefficients are predicted and are in agreement with experimental measurements. Consequently, the optimal reactor configuration giving the maximal oxygen supply is derived. Also, theoretical scaleup potential of this concentric internal loop reactor is considered for volumes ranging from 10 to 67,000 L with which cell densities of 5.1 x 10(7) and 1.2 x 10(7) cells/cm(3), respectively, can be maintained.
Related Concept Videos
Scale-Up Processes
Bioreactor Design and Operational System
Upstream Processing
Bioreactor Controls-II
Designing Growth Media for Bioreactors
Bioreactor Controls-III

