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  • The numerical results of the bubble size distribution and global gas hold-up are confronted with experimental data. The breakup model by Luo is shown to be strongly dependent on the discretization of the continuous size range of the bubble population. For correct gas hold-up prediction turbulent drag correction proved to be necessary.
  • The numerical results of the bubble size distribution and global gas hold-up are confronted with experimental data. The breakup model by Luo is shown to be strongly dependent on the discretization of the continuous size range of the bubble population. For correct gas hold-up prediction turbulent drag correction proved to be necessary. (en)
Title
  • Experimental measurement and CFD modelling of bubble size distribution in an aerated stirred tank
  • Experimental measurement and CFD modelling of bubble size distribution in an aerated stirred tank (en)
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  • Experimental measurement and CFD modelling of bubble size distribution in an aerated stirred tank
  • Experimental measurement and CFD modelling of bubble size distribution in an aerated stirred tank (en)
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  • RIV/60461373:22340/11:43892293!RIV12-MSM-22340___
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  • P(GA104/09/1290), P(GD104/08/H055), S, Z(MSM6046137306)
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  • 198782
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  • RIV/60461373:22340/11:43892293
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  • stirred tank; gas-liquid; gas hold-up; MUSIG; Bubble size distribution (en)
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  • [98FD13158148]
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  • Minneapolis
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  • Washington
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  • 2011 AIChE Fall Annual Meeting
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  • Jahoda, Milan
  • Kálal, Zbyněk
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  • American Chemical Society
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  • 978-0-8169-1070-0
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  • 22340
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