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    Assessment of Drag Models for Geldart A Particles in Bubbling Fluidized Beds

    Source: Journal of Fluids Engineering:;2016:;volume( 138 ):;issue: 003::page 31105
    Author:
    Estejab, Bahareh
    ,
    Battaglia, Francine
    DOI: 10.1115/1.4031490
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: 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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      Assessment of Drag Models for Geldart A Particles in Bubbling Fluidized Beds

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    contributor authorEstejab, Bahareh
    contributor authorBattaglia, Francine
    date accessioned2017-05-09T01:29:22Z
    date available2017-05-09T01:29:22Z
    date issued2016
    identifier issn0098-2202
    identifier otherfe_138_03_031105.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/161326
    description abstractIn 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.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleAssessment of Drag Models for Geldart A Particles in Bubbling Fluidized Beds
    typeJournal Paper
    journal volume138
    journal issue3
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.4031490
    journal fristpage31105
    journal lastpage31105
    identifier eissn1528-901X
    treeJournal of Fluids Engineering:;2016:;volume( 138 ):;issue: 003
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
    نرم افزار کتابخانه دیجیتال "دی اسپیس" فارسی شده توسط یابش برای کتابخانه های ایرانی | تماس با یابش
    yabeshDSpacePersian