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高等学校化学研究 ›› 2002, Vol. 18 ›› Issue (2): 113-116.

• Articles • 上一篇    下一篇

Numerical Simulation of Mixing in a Micro-well Scale Bioreactor by Computational Fluid Dynamics

Hu Zhang, Sally Lamping, Parviz Ayazi Shamlou   

  1. Advanced Biochemical Engineering Centre, University College London, Torrington Place, London, WC1E 7JE
  • 收稿日期:2001-11-25 出版日期:2002-04-24 发布日期:2011-08-04
  • 基金资助:

    Supported by UCL ORS Award and KC Wong Scholarship.

Numerical Simulation of Mixing in a Micro-well Scale Bioreactor by Computational Fluid Dynamics

Hu Zhang, Sally Lamping, Parviz Ayazi Shamlou   

  1. Advanced Biochemical Engineering Centre, University College London, Torrington Place, London, WC1E 7JE
  • Received:2001-11-25 Online:2002-04-24 Published:2011-08-04
  • Supported by:

    Supported by UCL ORS Award and KC Wong Scholarship.

摘要: The introduction of the multi-well plate miniaturisation technology with its associated automated dispensers, readers and integrated systems coupled with advances in life sciences has a propelling effect on the rate at which new potential drug molecules are discovered. The translation of these discoveries to real outcome now demands parallel approaches which allow large numbers of process options to be rapidly assessed. The engineering challenges in achieving this provide the motivation for the proposed work. In this work we used computational fluid dynamics(CFD) analysis to study flow conditions in a gas-liquid contactor which has the potential to be used as a fermenter on a multi-well format. The bioreactor had a working volume of 6.5 mL with the major dimensions equal to those of a single well of a 24-well plate. The 6.5 mL bioreactor was mechanically agitated and aerated by a single sparger placed beneath the bottom impeller. Detailed numerical procedure for solving the governing flow equations is given. The CFD results are combined with population balance equations to establish the size of the bubbles and their distribution in the bioreactor, Power curves with and without aeration are provided based on the simulated results.

关键词: CFD, Numerical simulation, Fermenter, Snapshot method, Two-fluid, Population balance

Abstract: The introduction of the multi-well plate miniaturisation technology with its associated automated dispensers, readers and integrated systems coupled with advances in life sciences has a propelling effect on the rate at which new potential drug molecules are discovered. The translation of these discoveries to real outcome now demands parallel approaches which allow large numbers of process options to be rapidly assessed. The engineering challenges in achieving this provide the motivation for the proposed work. In this work we used computational fluid dynamics(CFD) analysis to study flow conditions in a gas-liquid contactor which has the potential to be used as a fermenter on a multi-well format. The bioreactor had a working volume of 6.5 mL with the major dimensions equal to those of a single well of a 24-well plate. The 6.5 mL bioreactor was mechanically agitated and aerated by a single sparger placed beneath the bottom impeller. Detailed numerical procedure for solving the governing flow equations is given. The CFD results are combined with population balance equations to establish the size of the bubbles and their distribution in the bioreactor, Power curves with and without aeration are provided based on the simulated results.

Key words: CFD, Numerical simulation, Fermenter, Snapshot method, Two-fluid, Population balance