Show simple item record

contributor authorArnaud Delebarre
date accessioned2017-05-09T00:07:43Z
date available2017-05-09T00:07:43Z
date copyrightSeptember, 2002
date issued2002
identifier issn0098-2202
identifier otherJFEGA4-27175#595_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/126934
description abstractThis work proposes an equation giving the pressure drop of a gas flowing through a porous medium or a granular bed. The consequences for the onset of the fluidization are then discussed. It appears that the notion of minimum gas mass-flow rate would improve the description of the transition between fixed and fluidized bed regimes. An equation is then proposed to calculate the minimum fluidization gas mass-flow rate. It is then proved that the minimum fluidization is not only a function of the medium and fluid characteristics but also that it increases with bed inventory. It is then shown that a batch of particles has a minimum fluidization depending on its arrangement in a column and that in some cases, this minimum does not exist at all. As a consequence, the minimum of fluidization, whether it is a velocity or a mass flow rate, cannot be considered as a criterion to characterize a powder.
publisherThe American Society of Mechanical Engineers (ASME)
titleDoes the Minimum Fluidization Exist?
typeJournal Paper
journal volume124
journal issue3
journal titleJournal of Fluids Engineering
identifier doi10.1115/1.1490377
journal fristpage595
journal lastpage600
identifier eissn1528-901X
keywordsParticulate matter
keywordsFluidization
keywordsEquations
keywordsFlow (Dynamics)
keywordsPressure
keywordsFluids AND Pressure drop
treeJournal of Fluids Engineering:;2002:;volume( 124 ):;issue: 003
contenttypeFulltext


Files in this item

Thumbnail

This item appears in the following Collection(s)

Show simple item record