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    The Flow of Non-Newtonian Fluids on a Flat Plate With a Uniform Heat Flux

    Source: Journal of Heat Transfer:;2009:;volume( 131 ):;issue: 001::page 11702
    Author:
    M. M. Molla
    ,
    L. S. Yao
    DOI: 10.1115/1.2977610
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Forced convective heat transfer of non-Newtonian fluids on a flat plate with the heating condition of uniform surface heat flux has been investigated using a modified power-law viscosity model. This model does not restrain physically unrealistic limits; consequently, no irremovable singularities are introduced into a boundary-layer formulation for power-law non-Newtonian fluids. Therefore, the boundary-layer equations can be solved by marching from leading edge to downstream as any Newtonian fluids. For shear-thinning and shear-thickening fluids, non-Newtonian effects are illustrated via velocity and temperature distributions, shear stresses, and local temperature distribution. Most significant effects occur near the leading edge, gradually tailing off far downstream where the variation in shear stresses becomes smaller.
    keyword(s): Flow (Dynamics) , Fluids , Viscosity , Shear (Mechanics) , Non-Newtonian fluids , Boundary layers , Equations , Flat plates , Heat flux , Temperature distribution AND Stress ,
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      The Flow of Non-Newtonian Fluids on a Flat Plate With a Uniform Heat Flux

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    http://yetl.yabesh.ir/yetl1/handle/yetl/141147
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    contributor authorM. M. Molla
    contributor authorL. S. Yao
    date accessioned2017-05-09T00:33:57Z
    date available2017-05-09T00:33:57Z
    date copyrightJanuary, 2009
    date issued2009
    identifier issn0022-1481
    identifier otherJHTRAO-27853#011702_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/141147
    description abstractForced convective heat transfer of non-Newtonian fluids on a flat plate with the heating condition of uniform surface heat flux has been investigated using a modified power-law viscosity model. This model does not restrain physically unrealistic limits; consequently, no irremovable singularities are introduced into a boundary-layer formulation for power-law non-Newtonian fluids. Therefore, the boundary-layer equations can be solved by marching from leading edge to downstream as any Newtonian fluids. For shear-thinning and shear-thickening fluids, non-Newtonian effects are illustrated via velocity and temperature distributions, shear stresses, and local temperature distribution. Most significant effects occur near the leading edge, gradually tailing off far downstream where the variation in shear stresses becomes smaller.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleThe Flow of Non-Newtonian Fluids on a Flat Plate With a Uniform Heat Flux
    typeJournal Paper
    journal volume131
    journal issue1
    journal titleJournal of Heat Transfer
    identifier doi10.1115/1.2977610
    journal fristpage11702
    identifier eissn1528-8943
    keywordsFlow (Dynamics)
    keywordsFluids
    keywordsViscosity
    keywordsShear (Mechanics)
    keywordsNon-Newtonian fluids
    keywordsBoundary layers
    keywordsEquations
    keywordsFlat plates
    keywordsHeat flux
    keywordsTemperature distribution AND Stress
    treeJournal of Heat Transfer:;2009:;volume( 131 ):;issue: 001
    contenttypeFulltext
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