Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analyses

This article is on the dimensional analysis and the classification of fluidization from the viewpoint of numerical analysis. At first, the governing equations used in the DEM (Discrete Element Method) and CFD (Computational Fluid Dynamics) coupling model was non-dimensionalized with the method of He...

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Main Authors: Azri, Alias, Kuwagi, Kenya, Kogane, Atsuto, Hirano, Hiroyuki, Takami, Toshihiro
Format: Article
Language:English
Published: Elsevier 2014
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Online Access:http://umpir.ump.edu.my/id/eprint/7982/1/Non-Dimensionalization%20and%20Three-Dimensional%20Flow%20Regime%20Map%20for%20Fluidization%20Analyses.pdf
http://umpir.ump.edu.my/id/eprint/7982/
http://dx.doi.org/10.1016/j.ces.2014.08.006
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spelling my.ump.umpir.79822016-01-19T04:24:14Z http://umpir.ump.edu.my/id/eprint/7982/ Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analyses Azri, Alias Kuwagi, Kenya Kogane, Atsuto Hirano, Hiroyuki Takami, Toshihiro TP Chemical technology TA Engineering (General). Civil engineering (General) This article is on the dimensional analysis and the classification of fluidization from the viewpoint of numerical analysis. At first, the governing equations used in the DEM (Discrete Element Method) and CFD (Computational Fluid Dynamics) coupling model was non-dimensionalized with the method of Hellums and Churchill (1964). From the resulting dimensionless equations, it was concluded that the five dimensionless numbers, i.e. Re: Reynolds number, Ar: Archimedes number, Ga: Galilei number, Fr: Froude number and �*: ratio of particle density divided by fluid density, can be derived and hydrodynamically dominant on the fluid behaviors. Further, these can illustrate the dimensionless numbers proposed in the previous studies. Secondary, a three-dimensional flow regime map of homogeneous, bubbling and turbulent fluidizations was proposed with these dimensionless numbers using the DEM-CFD simulations. Finally, the plane of the minimum bubbling fluidization velocity umb in the map can be proposed and expressed as,�Re�_mb=0.263�^(*-0.553) �Ar�^0.612. umb can be estimated using this equation for various conditions. Elsevier 2014-08-13 Article PeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/7982/1/Non-Dimensionalization%20and%20Three-Dimensional%20Flow%20Regime%20Map%20for%20Fluidization%20Analyses.pdf Azri, Alias and Kuwagi, Kenya and Kogane, Atsuto and Hirano, Hiroyuki and Takami, Toshihiro (2014) Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analyses. Chemical Engineering Science, 119. pp. 199-211. ISSN 0009-2509 http://dx.doi.org/10.1016/j.ces.2014.08.006 DOI: 10.1016/j.ces.2014.08.006
institution Universiti Malaysia Pahang
building UMP Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaysia Pahang
content_source UMP Institutional Repository
url_provider http://umpir.ump.edu.my/
language English
topic TP Chemical technology
TA Engineering (General). Civil engineering (General)
spellingShingle TP Chemical technology
TA Engineering (General). Civil engineering (General)
Azri, Alias
Kuwagi, Kenya
Kogane, Atsuto
Hirano, Hiroyuki
Takami, Toshihiro
Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analyses
description This article is on the dimensional analysis and the classification of fluidization from the viewpoint of numerical analysis. At first, the governing equations used in the DEM (Discrete Element Method) and CFD (Computational Fluid Dynamics) coupling model was non-dimensionalized with the method of Hellums and Churchill (1964). From the resulting dimensionless equations, it was concluded that the five dimensionless numbers, i.e. Re: Reynolds number, Ar: Archimedes number, Ga: Galilei number, Fr: Froude number and �*: ratio of particle density divided by fluid density, can be derived and hydrodynamically dominant on the fluid behaviors. Further, these can illustrate the dimensionless numbers proposed in the previous studies. Secondary, a three-dimensional flow regime map of homogeneous, bubbling and turbulent fluidizations was proposed with these dimensionless numbers using the DEM-CFD simulations. Finally, the plane of the minimum bubbling fluidization velocity umb in the map can be proposed and expressed as,�Re�_mb=0.263�^(*-0.553) �Ar�^0.612. umb can be estimated using this equation for various conditions.
format Article
author Azri, Alias
Kuwagi, Kenya
Kogane, Atsuto
Hirano, Hiroyuki
Takami, Toshihiro
author_facet Azri, Alias
Kuwagi, Kenya
Kogane, Atsuto
Hirano, Hiroyuki
Takami, Toshihiro
author_sort Azri, Alias
title Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analyses
title_short Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analyses
title_full Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analyses
title_fullStr Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analyses
title_full_unstemmed Non-dimensionalization and Three-dimensional Flow Regime Map for Fluidization Analyses
title_sort non-dimensionalization and three-dimensional flow regime map for fluidization analyses
publisher Elsevier
publishDate 2014
url http://umpir.ump.edu.my/id/eprint/7982/1/Non-Dimensionalization%20and%20Three-Dimensional%20Flow%20Regime%20Map%20for%20Fluidization%20Analyses.pdf
http://umpir.ump.edu.my/id/eprint/7982/
http://dx.doi.org/10.1016/j.ces.2014.08.006
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score 13.160551