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    Heat Transfer in the Flow of Gases Around Oil Sand Spheres

    Source: Journal of Energy Resources Technology:;1988:;volume( 110 ):;issue: 004::page 276
    Author:
    M. A. Abdrabboh
    ,
    G. A. Karim
    DOI: 10.1115/1.3231393
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: An experimental study was conducted for the combined free and forced convection heating of preshaped molded spherical particles of Athabasca oil sands in hot gaseous streams of air at low Reynolds numbers. Based on a quasi-steady system, the lumped-heat-capacity approximation was employed to estimate the heat transfer coefficient of the transient convective system for each prescribed set of experimental stream conditions. Correlation of the results was made in terms of the dimensionless Nusselt number as a function of the particle Reynolds number and a dimensionless temperature difference. The simple closed-form analytical expression of the correlation was shown to fit the experimental data well.
    keyword(s): Heat transfer , Gases , Sands , Flow (Dynamics) , Particulate matter , Reynolds number , Mixed convection , Approximation , Heating , Heat transfer coefficients , Heat AND Temperature ,
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      Heat Transfer in the Flow of Gases Around Oil Sand Spheres

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/103780
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    • Journal of Energy Resources Technology

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    contributor authorM. A. Abdrabboh
    contributor authorG. A. Karim
    date accessioned2017-05-08T23:26:58Z
    date available2017-05-08T23:26:58Z
    date copyrightDecember, 1988
    date issued1988
    identifier issn0195-0738
    identifier otherJERTD2-26424#276_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/103780
    description abstractAn experimental study was conducted for the combined free and forced convection heating of preshaped molded spherical particles of Athabasca oil sands in hot gaseous streams of air at low Reynolds numbers. Based on a quasi-steady system, the lumped-heat-capacity approximation was employed to estimate the heat transfer coefficient of the transient convective system for each prescribed set of experimental stream conditions. Correlation of the results was made in terms of the dimensionless Nusselt number as a function of the particle Reynolds number and a dimensionless temperature difference. The simple closed-form analytical expression of the correlation was shown to fit the experimental data well.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleHeat Transfer in the Flow of Gases Around Oil Sand Spheres
    typeJournal Paper
    journal volume110
    journal issue4
    journal titleJournal of Energy Resources Technology
    identifier doi10.1115/1.3231393
    journal fristpage276
    journal lastpage278
    identifier eissn1528-8994
    keywordsHeat transfer
    keywordsGases
    keywordsSands
    keywordsFlow (Dynamics)
    keywordsParticulate matter
    keywordsReynolds number
    keywordsMixed convection
    keywordsApproximation
    keywordsHeating
    keywordsHeat transfer coefficients
    keywordsHeat AND Temperature
    treeJournal of Energy Resources Technology:;1988:;volume( 110 ):;issue: 004
    contenttypeFulltext
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