4.7 Article

Fluidization dynamics of wet Geldart D particles by pressure fluctuation analysis

Journal

POWDER TECHNOLOGY
Volume 388, Issue -, Pages 450-461

Publisher

ELSEVIER
DOI: 10.1016/j.powtec.2021.04.078

Keywords

Wet particles; Fluidization; Pressure fluctuations; Slugging; Defluidization

Funding

  1. Major Program of the National Natural Science Foundation of China [51576046]
  2. National Natural Science Foundation of China [51906092]

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This study discusses the effects of liquid saturation, gas velocity, and particle size on the global fluidization dynamics of Geldart D particles, finding that increasing liquid saturation and decreasing particle size intensifies bubble dynamics, with changes in fluidization regimes as gas velocity increases.
The increase of liquid saturation badly affects the fluidization dynamics, even resulting in the failure of fluidiza-tion. Nevertheless, few researches focus on characterizing the flow pattern transition of wet particles. In this work, we discuss the effects of the liquid saturation, gas velocity and the particle size on the global fluidization dynamics of Geldart D particles by analyzing the pressure fluctuations in the fluidized bed. The results show that the bubble dynamics is intensified with the increasing liquid saturation and decreasing particle size. When the superficial gas velocity increases, the fluidization regimes change from expanding regime, to multi-bubbling regime and slugging. During the normal fluidization and slugging, the liquid bridge forces prevent the growth of large bubbles and promote the probability of bubble break-up. Thus, the average bubble size de-creases and the number of bubbles increases, which lead to the intense bubble behavior. With the decreasing par-ticle size, the effect of liquid bridge forces is enhanced, contributing to the intensified bubble dynamics, including fast rising, frequent coalescence and eruption of a large number of bubbles. Compared to dry particles, wet par-ticles are easily to cause defluidization when the gas velocity is small. The PSD patterns have the sharp narrow peaks at frequency lower than 0.8 Hz. When the liquid saturation is increased to 30%, a gas channel forms in the bed, which resists the normal works of the fluidized bed. Basically, reducing the liquid saturation isa reason-able way to avoid defluidization. (c) 2021 Elsevier B.V. All rights reserved.

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