Modeling and design of optimal flow perfusion bioreactors for tissue engineering applications
| Autor: | Sarah L Griffiths, Sarah H. Cartmell, Shailesh Naire, Sundaramoorthy Thirunavukkarasu, L. Araida Hidalgo-Bastida |
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| Rok vydání: | 2011 |
| Předmět: |
Materials science
Flow (psychology) Bioengineering Computational fluid dynamics Applied Microbiology and Biotechnology Permeability Bioreactors Tissue engineering Shear stress Bioreactor Computer Simulation Cells Cultured geography geography.geographical_feature_category Tissue Engineering Tissue Scaffolds Viscosity business.industry Optimal flow technology industry and agriculture Equipment Design Mechanics Models Theoretical Inlet Culture Media Perfusion Hydrodynamics Modeling and design business Porosity Cell Division Biotechnology |
| Zdroj: | Biotechnology and Bioengineering. 109:1095-1099 |
| ISSN: | 0006-3592 |
| Popis: | Perfusion bioreactors have been used in different tissue engineering applications because of their consistent distribution of nutrients and flow-induced shear stress within the tissue-engineering scaffold. A widely used configuration uses a scaffold with a circular cross-section enclosed within a cylindrical chamber and inlet and outlet pipes which are connected to the chamber on either side through which media is continuously circulated. However, fluid-flow experiments and simulations have shown that the majority of the flow perfuses through the center. This pattern creates stagnant zones in the peripheral regions as well as in those of high flow rate near the inlet and outlet. This non-uniformity of flow and shear stress, owing to a circular design, results in limited cell proliferation and differentiation in these areas. The focus of this communication is to design an optimized perfusion system using computational fluid dynamics as a mathematical tool to overcome the time-consuming trial and error experimental method. We compared the flow within a circular and a rectangular bioreactor system. Flow simulations within the rectangular bioreactor are shown to overcome the limitations in the circular design. This communication challenges the circular cross-section bioreactor configuration paradigm and provides proof of the advantages of the new design over the existing one. Biotechnol. Bioeng. 2012; 109:1095–1099. © 2011 Wiley Periodicals, Inc. |
| Databáze: | OpenAIRE |
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