Tomographic analysis of dry and semi-wet bed fluidization

The effect of small liquid loading and particle size on the bubbling behaviour

Yassir T. Makkawi, Phillip C. Wright

Research output: Contribution to journalArticle

Abstract

The hydrodynamic changes resulting from the addition of very small quantities of a non-volatile liquid into a cold conventional fluidized bed has been investigated, and compared with the effects of increasing the particle size in a dry bed. Three different particle mixtures belonging to Group A/B, Group B and Group B/D were assessed. The changes in regime transition velocities, pressure drop, bubble rise velocity, bubble frequency and bubble flow rate have been quantified by employing Electrical Capacitance Tomography measurements. A new analysis method for measuring the effective interparticle forces (Fip) and the effective drag force (Fd) in a dry fluidized bed is described, and the results are presented in terms of different force ratios including the single particle weight (W). It is shown that the addition of a few drops of liquid (<0.055 wt%) to a dry bed of Group B or B/D introduces similar hydrodynamic changes (except, in terms of bubble frequency) as that of increasing the bed particle size, and these particular changes shift the powders away from Group A/B behaviour. It is also illustrated that for beds of different particle sizes, a typical bubbling behaviour can be achieved at a specific gas velocity, this velocity coincides with the point of equality in hydrodynamic force ratios Fd/W, Fip/W and Eip/Fd. © 2003 Elsevier Ltd. All rights reserved.

Original languageEnglish
Pages (from-to)201-213
Number of pages13
JournalChemical Engineering Science
Volume59
Issue number1
DOIs
Publication statusPublished - Jan 2004

Fingerprint

beds
bubbles
liquids
hydrodynamics
pressure drop
drag
flow velocity
tomography
capacitance
shift
gases

Keywords

  • Bubble characteristics
  • Electrical capacitance tomography
  • Interparticle force
  • Powder characteristics
  • Wet bed

Cite this

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abstract = "The hydrodynamic changes resulting from the addition of very small quantities of a non-volatile liquid into a cold conventional fluidized bed has been investigated, and compared with the effects of increasing the particle size in a dry bed. Three different particle mixtures belonging to Group A/B, Group B and Group B/D were assessed. The changes in regime transition velocities, pressure drop, bubble rise velocity, bubble frequency and bubble flow rate have been quantified by employing Electrical Capacitance Tomography measurements. A new analysis method for measuring the effective interparticle forces (Fip) and the effective drag force (Fd) in a dry fluidized bed is described, and the results are presented in terms of different force ratios including the single particle weight (W). It is shown that the addition of a few drops of liquid (<0.055 wt{\%}) to a dry bed of Group B or B/D introduces similar hydrodynamic changes (except, in terms of bubble frequency) as that of increasing the bed particle size, and these particular changes shift the powders away from Group A/B behaviour. It is also illustrated that for beds of different particle sizes, a typical bubbling behaviour can be achieved at a specific gas velocity, this velocity coincides with the point of equality in hydrodynamic force ratios Fd/W, Fip/W and Eip/Fd. {\circledC} 2003 Elsevier Ltd. All rights reserved.",
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Tomographic analysis of dry and semi-wet bed fluidization : The effect of small liquid loading and particle size on the bubbling behaviour. / Makkawi, Yassir T.; Wright, Phillip C.

In: Chemical Engineering Science, Vol. 59, No. 1, 01.2004, p. 201-213.

Research output: Contribution to journalArticle

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