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    Hydrodynamics of Two-Phase Flow Across Horizontal In-line and Staggered Rod Bundles

    Source: Journal of Fluids Engineering:;1992:;volume( 114 ):;issue: 003::page 450
    Author:
    R. Dowlati
    ,
    A. M. C. Chan
    ,
    M. Kawaji
    DOI: 10.1115/1.2910052
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: The void fraction and friction pressure drop measurements have been made for vertical two-phase flow of air-water across staggered and in-line rod bundles with different pitch-to-diameter ratios. All void fraction data showed a strong mass velocity effect and were significantly less than the values predicted by a homogeneous flow model, but were well correlated using the dimensionless gas velocity, jg * . The two-phase friction multiplier data could be well correlated with the Martinelli parameter for G > 200 kg/m2 s. The correlations developed for void fraction and two-phase friction multiplier were successfully tested in predicting the total pressure drop in boiling R-113 experiments.
    keyword(s): Hydrodynamics , Two-phase flow , Fuel rods , Porosity , Friction , Pressure drop , Water , Measurement , Boiling AND Flow (Dynamics) ,
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      Hydrodynamics of Two-Phase Flow Across Horizontal In-line and Staggered Rod Bundles

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/110432
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    • Journal of Fluids Engineering

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    contributor authorR. Dowlati
    contributor authorA. M. C. Chan
    contributor authorM. Kawaji
    date accessioned2017-05-08T23:38:46Z
    date available2017-05-08T23:38:46Z
    date copyrightSeptember, 1992
    date issued1992
    identifier issn0098-2202
    identifier otherJFEGA4-27069#450_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/110432
    description abstractThe void fraction and friction pressure drop measurements have been made for vertical two-phase flow of air-water across staggered and in-line rod bundles with different pitch-to-diameter ratios. All void fraction data showed a strong mass velocity effect and were significantly less than the values predicted by a homogeneous flow model, but were well correlated using the dimensionless gas velocity, jg * . The two-phase friction multiplier data could be well correlated with the Martinelli parameter for G > 200 kg/m2 s. The correlations developed for void fraction and two-phase friction multiplier were successfully tested in predicting the total pressure drop in boiling R-113 experiments.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleHydrodynamics of Two-Phase Flow Across Horizontal In-line and Staggered Rod Bundles
    typeJournal Paper
    journal volume114
    journal issue3
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.2910052
    journal fristpage450
    journal lastpage456
    identifier eissn1528-901X
    keywordsHydrodynamics
    keywordsTwo-phase flow
    keywordsFuel rods
    keywordsPorosity
    keywordsFriction
    keywordsPressure drop
    keywordsWater
    keywordsMeasurement
    keywordsBoiling AND Flow (Dynamics)
    treeJournal of Fluids Engineering:;1992:;volume( 114 ):;issue: 003
    contenttypeFulltext
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