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Hydrodynamics and Mass Transfer Performance of Turbulent Contact Absorbers

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Abstract

Operating velocities, pressure drop, liquid hold up and operating bed heights for TCA and packed bed contactors have been investigated fora wide range of operating conditions. A model for counter-current gas-liquid contacting in a bed of spherical packing is proposed. Two operating regimes, the fluidization before flooding (type I TCA) and fluidization at the flooding point of a fixed bed (type II TCA) are described and predicted by a phase diagram. A correlation for minimum fluidization velocity is presented, based on the proposed hydrodynamical model.

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© 1980 Plenum Press, New York

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Vunjak-Novaković, G.V., Vuković, D.V., Obermayer, A., Vogelpohl, A. (1980). Hydrodynamics and Mass Transfer Performance of Turbulent Contact Absorbers. In: Grace, J.R., Matsen, J.M. (eds) Fluidization. Springer, Boston, MA. https://doi.org/10.1007/978-1-4684-1045-7_23

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  • DOI: https://doi.org/10.1007/978-1-4684-1045-7_23

  • Publisher Name: Springer, Boston, MA

  • Print ISBN: 978-1-4684-1047-1

  • Online ISBN: 978-1-4684-1045-7

  • eBook Packages: Springer Book Archive

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