Models for Predicting Average Bubble Diameter and Volumetric Bubble Flux in Deep Fluidized Beds-Reference-Cited by-同舟云学术

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Models for Predicting Average Bubble Diameter and Volumetric Bubble Flux in Deep Fluidized Beds

Published:2018-02-01 Issue:7 Volume:57 Page:2658-2669
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Agu Cornelius E.¹^ORCID,Pfeifer Christoph²,Eikeland Marianne¹,Tokheim Lars-Andre¹,Moldestad Britt M. E.¹

Affiliation:

1. Department of Process, Energy, and Environmental Technology, University College of Southeast Norway, 3918 Porsgrunn, Norway

2. Department of Material Sciences and Process Engineering, University of Natural Resources and Life Sciences, 1190 Vienna, Austria

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

http://pubs.acs.org/doi/pdf/10.1021/acs.iecr.7b04370

Reference37 articles.

1. Types of gas fluidization

2. Hydrodynamics of beds of small particles in the voids of coarse particles

3. Bubble size and frequency in gas fluidized beds.

4. Estimation of bubble diameter in gaseous fluidized beds

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1. On Bubble–Jet Interactions in Fluidized Beds;Industrial & Engineering Chemistry Research;2024-05-08

2. Wet fluidization characterization of potash particles in a pulsation-assisted fluidized bed;Powder Technology;2023-10

3. Fluidization and bubbling behavior of potash particles in a deep fluidized bed;Particuology;2023-09

4. 3D CFD-PBM simulation of gas–solid bubbling beds of Geldart A particles with sub-grid drag correction;Chemical Engineering Science;2023-07

5. Study of Fluidization Behavior Transition from Geldart B to A Induced by High Temperature Using Electrical Capacitance Tomography;Industrial & Engineering Chemistry Research;2023-05-31

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