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    Two-Phase Void Fraction and Pressure Drop in Horizontal Crossflow Across a Tube Bundle

    Source: Journal of Fluids Engineering:;1998:;volume( 120 ):;issue: 001::page 140
    Author:
    G. P. Xu
    ,
    K. W. Tou
    ,
    C. P. Tso
    DOI: 10.1115/1.2819638
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Void fraction and friction pressure drop measurements were made for an adiabatic, horizontal two-phase flow of air-water, air-oil across a horizontal in-line, 5 × 20 tube bundle with pitch-to-diameter ratio, P/D, of 1.28. For both air-water and air-oil flow, the experimental results showed that the average void fraction were less than the values predicted by a homogenous flow model, but were well correlated with the Martinelli parameter Xtt and liquid-only Froude number FrLO . The two-phase friction multiplier data exhibited an effect of flow pattern and mass velocity, and they could be well-correlated with the Martinelli parameter.
    keyword(s): Porosity , Pressure drop , Flow (Dynamics) , Friction , Water , Measurement AND Two-phase flow ,
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      Two-Phase Void Fraction and Pressure Drop in Horizontal Crossflow Across a Tube Bundle

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/120687
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    contributor authorG. P. Xu
    contributor authorK. W. Tou
    contributor authorC. P. Tso
    date accessioned2017-05-08T23:57:04Z
    date available2017-05-08T23:57:04Z
    date copyrightMarch, 1998
    date issued1998
    identifier issn0098-2202
    identifier otherJFEGA4-27126#140_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/120687
    description abstractVoid fraction and friction pressure drop measurements were made for an adiabatic, horizontal two-phase flow of air-water, air-oil across a horizontal in-line, 5 × 20 tube bundle with pitch-to-diameter ratio, P/D, of 1.28. For both air-water and air-oil flow, the experimental results showed that the average void fraction were less than the values predicted by a homogenous flow model, but were well correlated with the Martinelli parameter Xtt and liquid-only Froude number FrLO . The two-phase friction multiplier data exhibited an effect of flow pattern and mass velocity, and they could be well-correlated with the Martinelli parameter.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleTwo-Phase Void Fraction and Pressure Drop in Horizontal Crossflow Across a Tube Bundle
    typeJournal Paper
    journal volume120
    journal issue1
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.2819638
    journal fristpage140
    journal lastpage145
    identifier eissn1528-901X
    keywordsPorosity
    keywordsPressure drop
    keywordsFlow (Dynamics)
    keywordsFriction
    keywordsWater
    keywordsMeasurement AND Two-phase flow
    treeJournal of Fluids Engineering:;1998:;volume( 120 ):;issue: 001
    contenttypeFulltext
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