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    Pressure Drop Correlations for Inclined Two-Phase Flow

    Source: Journal of Energy Resources Technology:;1985:;volume( 107 ):;issue: 004::page 549
    Author:
    H. Mukherjee
    ,
    J. P. Brill
    DOI: 10.1115/1.3231233
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Pressure drop behavior in two-phase inclined flow was studied. For bubble and slug flow, a no-slip friction factor calculated from the Moody diagram was found adequate for friction head loss calculations. In downhill stratified flow, the friction pressure gradient is calculated based on a momentum balance equation for either phase assuming a smooth gas-liquid interface. For this calculation, a prior knowledge of the liquid holdup is needed. For annular-mist flow, a friction factor correlation is presented that is a function of holdup ratio and no-slip Moody friction factor. Results agree well with the experimental data and correlations were further verified with Prudhoe Bay and North Sea data.
    keyword(s): Pressure drop , Two-phase flow , Friction , Flow (Dynamics) , Momentum , Bubbles , Pressure gradient , Slug , Stratified flow , North Sea AND Equations ,
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      Pressure Drop Correlations for Inclined Two-Phase Flow

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/99652
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    • Journal of Energy Resources Technology

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    contributor authorH. Mukherjee
    contributor authorJ. P. Brill
    date accessioned2017-05-08T23:19:52Z
    date available2017-05-08T23:19:52Z
    date copyrightDecember, 1985
    date issued1985
    identifier issn0195-0738
    identifier otherJERTD2-26408#549_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/99652
    description abstractPressure drop behavior in two-phase inclined flow was studied. For bubble and slug flow, a no-slip friction factor calculated from the Moody diagram was found adequate for friction head loss calculations. In downhill stratified flow, the friction pressure gradient is calculated based on a momentum balance equation for either phase assuming a smooth gas-liquid interface. For this calculation, a prior knowledge of the liquid holdup is needed. For annular-mist flow, a friction factor correlation is presented that is a function of holdup ratio and no-slip Moody friction factor. Results agree well with the experimental data and correlations were further verified with Prudhoe Bay and North Sea data.
    publisherThe American Society of Mechanical Engineers (ASME)
    titlePressure Drop Correlations for Inclined Two-Phase Flow
    typeJournal Paper
    journal volume107
    journal issue4
    journal titleJournal of Energy Resources Technology
    identifier doi10.1115/1.3231233
    journal fristpage549
    journal lastpage554
    identifier eissn1528-8994
    keywordsPressure drop
    keywordsTwo-phase flow
    keywordsFriction
    keywordsFlow (Dynamics)
    keywordsMomentum
    keywordsBubbles
    keywordsPressure gradient
    keywordsSlug
    keywordsStratified flow
    keywordsNorth Sea AND Equations
    treeJournal of Energy Resources Technology:;1985:;volume( 107 ):;issue: 004
    contenttypeFulltext
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