4.7 Article

Flow regime transition and liquid distribution in a 3D concurrent downflow three-phase moving bed

Journal

CHEMICAL ENGINEERING JOURNAL
Volume 416, Issue -, Pages -

Publisher

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2021.129174

Keywords

Three-phase moving bed; Flow regime transition; Liquid distribution; Dynamic liquid holdup; Empirical model

Funding

  1. ExxonMobil Research and Engineering Company
  2. National Natural Science Foundation of China [21808197]
  3. National Science Fund for Distinguished Young [21525627]

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The study found that with an increase in solid flow rate, the liquid distribution in a three-phase moving bed becomes more uniform, but as the solid flow rate further increases, the liquid distribution becomes uneven.
Based on a cold-flow experimental setup, the transition between trickle flow and pulse flow in a 3D concurrent downflow three-phase moving bed is investigated by the standard deviation of pressure drop and visual observations. Results show that at a constant gas flow rate, the trickle-to-pulse transition shifts to a higher liquid flow rate with the increasing solid flow rate because the particle moving inhibits the formation of local liquid blockage. Furthermore, an empirical model is proposed to fit the trickle-to-pulse transition boundary by correlating the dynamic liquid holdup at the boundary with the gas Reynolds number, the particle velocity, and the relative viscosity. Finally, the effects of the particle moving on the liquid distribution are investigated, which shows that the particle moving makes the liquid distribution more uniform when the solid flow rate is smaller than a certain value. But further increasing the solid flow rate, the liquid distribution becomes uneven.

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