In order to accurately predict the hydrodynamic behavior of gas and solid phases using an Eulerian–Eulerian approach, it is crucial to use appropriate drag models to capture the correct physics. In this study, the performance of seven drag models for fluidization of Geldart A particles of coal, poplar wood, and their mixtures was assessed. In spite of the previous findings that bode badly for using predominately Geldart B drag models for fine particles, the results of our study revealed that if static regions of mass in the fluidized beds are considered, these drag models work well with Geldart A particles. It was found that drag models derived from empirical relationships adopt better with Geldart A particles compared to drag models that were numerically developed. Overall, the Huilin–Gidaspow drag model showed the best performance for both single solid phases and binary mixtures, however, for binary mixtures, Wen–Yu model predictions were also accurate.
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March 2016
Research-Article
Assessment of Drag Models for Geldart A Particles in Bubbling Fluidized Beds
Bahareh Estejab,
Bahareh Estejab
Department of Mechanical Engineering (MC 0238),
Virginia Polytechnic Institute
and State University,
Goodwin Hall, Room 210,
635 Prices Fork Road (0238),
Blacksburg, VA 24061
e-mail: bestejab@vt.edu
Virginia Polytechnic Institute
and State University,
Goodwin Hall, Room 210,
635 Prices Fork Road (0238),
Blacksburg, VA 24061
e-mail: bestejab@vt.edu
Search for other works by this author on:
Francine Battaglia
Francine Battaglia
Fellow ASME
Department of Mechanical Engineering (MC 0238),
Virginia Polytechnic Institute
and State University,
Goodwin Hall, Room 227,
635 Prices Fork Road (0238),
Blacksburg, VA 24061
e-mail: fbattaglia@vt.edu
Department of Mechanical Engineering (MC 0238),
Virginia Polytechnic Institute
and State University,
Goodwin Hall, Room 227,
635 Prices Fork Road (0238),
Blacksburg, VA 24061
e-mail: fbattaglia@vt.edu
Search for other works by this author on:
Bahareh Estejab
Department of Mechanical Engineering (MC 0238),
Virginia Polytechnic Institute
and State University,
Goodwin Hall, Room 210,
635 Prices Fork Road (0238),
Blacksburg, VA 24061
e-mail: bestejab@vt.edu
Virginia Polytechnic Institute
and State University,
Goodwin Hall, Room 210,
635 Prices Fork Road (0238),
Blacksburg, VA 24061
e-mail: bestejab@vt.edu
Francine Battaglia
Fellow ASME
Department of Mechanical Engineering (MC 0238),
Virginia Polytechnic Institute
and State University,
Goodwin Hall, Room 227,
635 Prices Fork Road (0238),
Blacksburg, VA 24061
e-mail: fbattaglia@vt.edu
Department of Mechanical Engineering (MC 0238),
Virginia Polytechnic Institute
and State University,
Goodwin Hall, Room 227,
635 Prices Fork Road (0238),
Blacksburg, VA 24061
e-mail: fbattaglia@vt.edu
1Corresponding author.
Contributed by the Fluids Engineering Division of ASME for publication in the JOURNAL OF FLUIDS ENGINEERING. Manuscript received April 7, 2015; final manuscript received August 19, 2015; published online October 8, 2015. Assoc. Editor: John Abraham.
J. Fluids Eng. Mar 2016, 138(3): 031105 (12 pages)
Published Online: October 8, 2015
Article history
Received:
April 7, 2015
Revised:
August 19, 2015
Citation
Estejab, B., and Battaglia, F. (October 8, 2015). "Assessment of Drag Models for Geldart A Particles in Bubbling Fluidized Beds." ASME. J. Fluids Eng. March 2016; 138(3): 031105. https://doi.org/10.1115/1.4031490
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