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Journal ArticleDOI

Flow structure of the solids in a 3‐D gas–liquid–solid fluidized bed

TLDR
In this article, a 3D gas-liquid-solid fluidized bed was studied using a noninvasive radioactive-particle tracking (RPT) technique using a multisite detection of γ radiations emitted from a single radiolabeled tracer particle.
Abstract
Local and macroscopic solids flow structure and kinematics in a 3-D gas–liquid–solid fluidized bed were studied using a noninvasive radioactive-particle tracking (RPT) technique. Based on the multisite detection of γ radiations emitted from a single radiolabeled tracer particle freely moving in the fluidized bed, RPT permitted to obtain fast sampling of 3-D trajectories of the tracer, whose physical properties were similar to those of the solids inventory. These trajectories showed the detailed motion sequences of the solid particles as entrained in the bubble wakes, fluctuating randomly or sinking deterministically in the liquid–solid emulsion. Based on measurements done in the vortical-spiral flow regime, the dynamic solids flow structure inside a three-phase fluidized bed can be viewed as a three-zone core–annulus–annulus structure: (1) a central fast-bubble flow region with the particles swirling upward; (2) a vortical flow region around the velocity inversion point with the particles momentarily captured in emulsion vortices; and (3) a relatively bubble-free descending flow region where the particles spiral down between the velocity inversion point and vessel walls. Our solids flow structure of dense fluidized beds are similar to the flow structure of liquid and/or solid in lean fluidized beds (observed through laser sheeting imaging). Measured distributions of local ensemble-averaged particle velocities and turbulence intensities were consistent with the existence of a toroidal recirculatory solids flow pattern in the bed. Measured mean circumferential ensemble-averaged radial velocity was essentially zero throughout most of the bed. The solids flow turbulence field was nonisotropic, as radial turbulence intensities were generally lower than longitudinal turbulence intensities.

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Journal ArticleDOI

Multiphase catalytic reactors: a perspective on current knowledge and future trends

TL;DR: In this paper, a review of the physical parameters for various multiphase reactors is presented, focusing on gas-phase catalyzed processes with an emphasis on unsteady state operation.
Journal ArticleDOI

Multiphase reactors – revisited

TL;DR: The state of the art of our understanding of the phenomena occurring in three-phase reactors such as packed beds with two-phase #ow, slurry bubble columns and ebullated beds is summarized in this paper.
Journal ArticleDOI

Noninvasive Tomographic and Velocimetric Monitoring of Multiphase Flows

TL;DR: A condensed review of recent advances accomplished in the development and the applications of noninvasive tomographic and velocimetric measurement techniques to multiphase flows and systems is presented in this article.
Journal ArticleDOI

Measurement techniques in fluidized beds

Joachim Werther
- 01 Apr 1999 - 
TL;DR: In this paper, an overview is given on available measuring techniques for industrial routine measurements, mainly temperature and pressure drop measurements, and also some advanced techniques which are either still under development or which are particularly intended for academic investigations of basic fluidization phenomena.
Journal ArticleDOI

Bubble formation and dynamics in gas–liquid–solid fluidization—A review

TL;DR: In this paper, the authors summarize the salient characteristics of liquid, bubbles, and particles and their interactive behavior and dynamics in the process of bubble formation and bubble rising in gas-liquid-solid fluidization systems.
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