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Journal ArticleDOI

Gas exchange between the bubble and emulsion phases in gas-solid fluidized beds

Tadatoshi Chiba, +1 more
- 01 Sep 1970 - 
- Vol. 25, Iss: 9, pp 1375-1385
TLDR
In this article, the authors measured the extent of gas exchange between the bubble and emulsion phases in gas-solid fluidized beds using ozone as a tracer and found that the exchange coefficient values measured for single bubbles, as seen in this study, were found to be roughly one third of that obtained from freely bubbling fluidized bed, which fact was attributed to the coalescence of bubbles in the freely bubblebed.
About
This article is published in Chemical Engineering Science.The article was published on 1970-09-01. It has received 58 citations till now. The article focuses on the topics: Fluidized bed & Coalescence (physics).

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Citations
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Book ChapterDOI

Transport Phenomena and Reaction in Fluidized Catalyst Beds

TL;DR: In this article, a simplified theory for a bubble column is applied to understand particle circulation in the fluidized catalytic beds, and it is possible to analyze flow patterns of bubbles and emulsion.
Journal ArticleDOI

Gas Dispersion and Bubble-to-Emulsion Phase Mass Exchange in a Gas-Solid Bubbling Fluidized Bed: A Computational and Experimental Study

TL;DR: In this paper, the authors used a two-fluid model based on the Kinetic Theory of Granular Flow (KTGF) to predict the dispersion of tracer gas using a single bubble rising through an incipiently fluidized bed, revealing that the assumptions often made in phenomenological models in the derivation of correlations for the mass transfer coefficient, mainly that the bubble diameter remains constant and that the tracer concentration is uniform in the bubble, are not valid.
Journal ArticleDOI

Interphase mass transfer in an aggregative fluidized bed

TL;DR: The experimental technique developed by Chavarie and Grace has been used to measure interphase mass transfer rates for bubbles in a two-dimensional fluidized bed with different sizes of particles from 90 to 39O μm as discussed by the authors.
Journal ArticleDOI

Link between bubbling and segregation patterns in gas‐fluidized beds with continuous size distributions

TL;DR: In this article, experiments involving a bubble-less gas-fluidized bed with Gaussian and lognormal particle-size distributions of Geldart Group B particles have been carried out, with a focus on bubble measurements.
Journal ArticleDOI

Drying granular solids in a fluidized bed

TL;DR: In this paper, the authors presented a model which describes the mass transfer from the wet solids to a rising bubble for the case that there is no diffusion limitation inside the solids.
References
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Journal ArticleDOI

On the mathematics of fluidization Part 2. Steady motion of fully developed bubbles

TL;DR: In this paper, the momentum and mass conservation equations derived in part 1 are used in the limiting case of large solids-to-fluid density ratio in the presence of a fully developed bubble.
Journal ArticleDOI

Cloud formation around bubbles in gas fluidized beds

TL;DR: In this article, the shape and size of gas clouds as they form around bubbles in two-dimensional fluidized beds of spherical and irregular particles is described. And the behavior of clouds as their parent bubbles split and coalesce was described.
Journal ArticleDOI

Gas exchange between bubbles and dense phase in a fluidised bed

TL;DR: In this article, tracer-free air-flow at or slightly above the incipient fluidisation rate was used to produce a stream of bubbles containing tracer gas, which was injected continuously at a point near the distributor into fluidized beds, diameters 2 in. and 6 in.
Journal ArticleDOI

Reaction kinetics in fluidized beds

TL;DR: In this paper, the results obtained when using baffled beds show that the baffles improve the conversion from 10 per cent to 40 per cent over that obtained in non-baffled fluidized reactors.
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