Wave characterization for mammalian cell culture: residence time distribution.

The high dose requirements of biopharmaceutical products led to the development of mammalian cell culture technologies that increase biomanufacturing capacity. The disposable Wave bioreactor is one of the most promising technologies, providing ease of operation and no cross-contamination, and using an innovative undulation movement that ensures good mixing and oxygen transfer without cell damage. However, its recentness demands further characterization. This study evaluated the residence time distribution (RTD) in Wave, allowing the characterization of mixing and flow and the comparison with ideal models and a Stirred tank reactor (STR) used for mammalian cell culture. RTD was determined using methylene blue with pulse input methodology, at three flow rates common in mammalian cell culture (3.3×10(-5)m(3)/h, 7.9×10(-5)m(3)/h, and 1.25×10(-4)m(3)/h) and one typical of microbial culture (5×10(-3)m(3)/h). Samples were taken periodically and the absorbance read at 660nm. It was observed that Wave behavior diverted from ideal models, but was similar to STR. Therefore, the deviations are not related to the particular Wave rocking mechanism, but could be associated with the inadequacy of these reactors to operate in continuous mode or to a possible inability of the theoretical models to properly describe the behavior of reactors designed for mammalian cell culture. Thus, the development of new theoretical models could better characterize the performance of these reactors.

[1]  E. B. Nauman,et al.  Residence time distribution theory for unsteady stirred tank reactors , 1969 .

[2]  Wei-Shou Hu,et al.  Cell culture technology for pharmaceutical and cell-based therapies , 2005 .

[3]  J. P. Mmbaga,et al.  Introduction to Chemical Reactor Analysis , 2001 .

[4]  Athanassios Sambanis,et al.  Cell Culture Bioreactors , 2001 .

[5]  Sabine Geisse,et al.  Optimisation of protein expression and establishment of the Wave Bioreactor for Baculovirus/insect cell culture , 2004, Cytotechnology.

[6]  Regine Eibl,et al.  Bag bioreactor based on wave-induced motion: characteristics and applications. , 2009, Advances in biochemical engineering/biotechnology.

[7]  R. Bhatia,et al.  Growing Cholesterol‐Dependent NS0 Myeloma Cell Line in the Wave Bioreactor System: Overcoming Cholesterol‐Polymer Interaction by Using Pretreated Polymer or Inert Fluorinated Ethylene Propylene , 2005, Biotechnology progress.

[8]  P. V. Danckwerts The effect of incomplete mixing on homogeneous reactions , 1958 .

[9]  C. Ahmed Basha,et al.  Residence time distribution in continuous stirred tank electrochemical reactor , 2008 .

[10]  J. Fernández-Sempere,et al.  Residence time distribution for unsteady-state systems , 1995 .

[11]  Yusuf Chisti,et al.  Characterization of shear rates in airlift bioreactors for animal cell culture , 1997 .

[12]  Carla I.C. Pinheiro,et al.  Teaching Residence Time Distributions in the Laboratory , 2002 .

[13]  William Resnick,et al.  Residence Time Distribution in Real Systems , 1963 .

[14]  Udo Reichl,et al.  Characterization of flow conditions in 2 L and 20 L wave bioreactors® using computational fluid dynamics , 2010, Biotechnology progress.

[15]  Troy Shinbrot,et al.  Segregated regions in continuous laminar stirred tank reactors , 2004 .

[16]  O. Levenspiel Chemical Reaction Engineering , 1972 .

[17]  J. Turner The interpretation of residence-time measurements in systems with and without mixing , 1971 .

[18]  Ashraf Amanullah,et al.  Evaluation of a novel Wave Bioreactor® cellbag for aerobic yeast cultivation , 2007, Bioprocess and biosystems engineering.

[19]  F. Wurm Production of recombinant protein therapeutics in cultivated mammalian cells , 2004, Nature Biotechnology.

[20]  Vivek V. Ranade,et al.  Computational Flow Modeling for Chemical Reactor Engineering , 2001 .

[21]  Francesc Gòdia,et al.  Animal Cell Technology Meets Genomics , 2005 .

[22]  Regine Eibl,et al.  Growth and Ginsenoside Production in Hairy Root Cultures of Panax ginseng using a Novel Bioreactor , 2003, Planta medica.

[23]  Vijay P. Singh,et al.  Disposable bioreactor for cell culture using wave-induced agitation , 1999, Cytotechnology.

[24]  Terry A. Ring,et al.  Residence Time Distributions in a Stirred Tank: Comparison of CFD Predictions with Experiment , 2004 .

[25]  Hua Bai,et al.  Modeling flow and residence time distribution in an industrial-scale reactor with a plunging jet inlet and optional agitation , 2008 .

[26]  Regine Eibl,et al.  Design And Use Of The Wave Bioreactor For Plant Cell Culture , 2008 .

[27]  Stephan Kaiser,et al.  Disposable bioreactors: the current state-of-the-art and recommended applications in biotechnology , 2010, Applied Microbiology and Biotechnology.

[28]  Dieter Eibl,et al.  Disposable bioreactors in cell culture-based upstream processing , 2009 .

[29]  H. S. Fogler,et al.  Elements of Chemical Reaction Engineering , 1986 .