Literature DB >> 27690196

Studies on fluid dynamics of the flow field and gas transfer in orbitally shaken tubes.

Li-Kuan Zhu1,2, Bo-Yan Song1, Zhen-Long Wang1, Dominique T Monteil2, Xiao Shen2, David L Hacker2,3, Maria De Jesus4, Florian M Wurm2,4.   

Abstract

Orbitally shaken cylindrical bioreactors [OrbShake bioreactors (OSRs)] without an impeller or sparger are increasingly being used for the suspension cultivation of mammalian cells. Among small volume OSRs, 50-mL tubes with a ventilated cap (OSR50), originally derived from standard laboratory centrifuge tubes with a conical bottom, have found many applications including high-throughput screening for the optimization of cell cultivation conditions. To better understand the fluid dynamics and gas transfer rates at the liquid surface in OSR50, we established a three-dimensional simulation model of the unsteady liquid forms (waves) in this vessel. The studies verified that the operating conditions have a large effect on the interfacial surface. The volumetric mass transfer coefficient (kL a) was determined experimentally and from simulations under various working conditions. We also determined the liquid-phase mass transfer coefficient (kL ) and the specific interfacial area (a) under different conditions to demonstrate that the value of a affected the gas transfer rate more than did the value of kL . High oxygen transfer rates, sufficient for supporting the high-density culture of mammalian cells, were found. Finally, the average axial velocity of the liquid was identified to be an important parameter for maintaining cells in suspension. Overall these studies provide valuable insights into the preferable operating conditions for the OSR50, such as those needed for cell cultures requiring high oxygen levels.
© 2016 American Institute of Chemical Engineers Biotechnol. Prog., 33:192-200, 2017. © 2016 American Institute of Chemical Engineers.

Entities:  

Keywords:  CHO cells; cell suspension; computational fluid dynamics; orbitally shaken bioreactors; oxygen transfer rate

Mesh:

Substances:

Year:  2016        PMID: 27690196     DOI: 10.1002/btpr.2375

Source DB:  PubMed          Journal:  Biotechnol Prog        ISSN: 1520-6033


  3 in total

1.  Implementation of Perforated Concentric Ring Walls Considerably Improves Gas-Liquid Mass Transfer of Shaken Bioreactors.

Authors:  Sven Hansen; Andreas Gumprecht; Linda Micheel; Hans-Georg Hennemann; Franziska Enzmann; Wilfried Blümke
Journal:  Front Bioeng Biotechnol       Date:  2022-05-12

2.  Three-dimensional (3D) evaluation of liquid distribution in shake flask using an optical fluorescence technique.

Authors:  Amizon Azizan; Jochen Büchs
Journal:  J Biol Eng       Date:  2017-08-03       Impact factor: 4.355

3.  Designs and Characterization of Subunit Ebola GP Vaccine Candidates: Implications for Immunogenicity.

Authors:  Valentina Agnolon; Divor Kiseljak; Maria J Wurm; Florian M Wurm; Charlotte Foissard; Fabrice Gallais; Sarah Wehrle; César Muñoz-Fontela; Laurent Bellanger; Bruno Emanuel Correia; Giampietro Corradin; François Spertini
Journal:  Front Immunol       Date:  2020-11-04       Impact factor: 7.561

  3 in total

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