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  4. Solid-fluid mixing behavior of conical spouted beds with internal devices
 
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Solid-fluid mixing behavior of conical spouted beds with internal devices

Citation Link: https://doi.org/10.15480/882.8074
Publikationstyp
Journal Article
Date Issued
2023-09-01
Sprache
English
Author(s)
Achutegui Narbona, Aitor  orcid-logo
Feststoffverfahrenstechnik und Partikeltechnologie V-3  
Kieckhefen, Paul  orcid-logo
Feststoffverfahrenstechnik und Partikeltechnologie V-3  
Pietsch-Braune, Swantje  orcid-logo
Feststoffverfahrenstechnik und Partikeltechnologie V-3  
Aguado, Roberto  
Heinrich, Stefan  
Feststoffverfahrenstechnik und Partikeltechnologie V-3  
Olazar, Martin  
TORE-DOI
10.15480/882.8074
TORE-URI
https://hdl.handle.net/11420/42443
Journal
Advanced powder technology  
Volume
34
Issue
9
Start Page
1
End Page
11
Citation
Advanced Powder Technology 34 (9): 104136 (2023-09-01)
Publisher DOI
10.1016/j.apt.2023.104136
Scopus ID
2-s2.0-85162979161
Publisher
Elsevier
The effect of draft tubes and fountain confiner on the gas and solids mixing behavior is studied in conical spouted beds. Accordingly, the bed porosity has been determined in different hydrodynamic regimes of 1.1,1.25 and 1.5u/ums, with beds equipped with draft tubes of 0%,56% and 100% opening ratio. These devices significantly affect the gas residence time and particle cycle time distributions, which are further improved by using a fountain confiner, specially when high inlet gas flow rates are desired. The addition of this device was found to remove stagnant gas pockets over the annular zone, while reducing the particle cycle time by 15% with the OSDT configuration at 1.5u/ums. This reduction heavily depends on the distance between the bed surface and the fountain confiner. By including draft tubes, the expected particle cycle time can be more than doubled due to the reduced annular-spot solids circulation. Therefore, it was found that a combination of internal devices and operating flow rate present a promising strategy to control the gas flow pattern, while keeping the distribution of particles cycle times required for each application.
Subjects
CFD-DEM simulation
Gas-solid mixing
Particle cycle time
RTD
DDC Class
660: Chemistry; Chemical Engineering
Publication version
publishedVersion
Lizenz
https://creativecommons.org/licenses/by/4.0/
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