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    Correlation of Adiabatic Two-Phase Pressure Drop Data Using the Frictional Law of Corresponding States

    Source: Journal of Fluids Engineering:;1993:;volume( 115 ):;issue: 002::page 317
    Author:
    N. T. Obot
    ,
    M. W. Wambsganss
    ,
    D. M. France
    ,
    J. A. Jendrzejczyk
    DOI: 10.1115/1.2910141
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: A method, based on that developed for single-phase flow, is proposed for the correlation of two-phase frictional pressure drop data. It is validated using air-water data obtained on small horizontal passages of rectangular and circular cross-section for values of total mass flux G in the 50-2000 kg/m2 s range. The pressure drop for air-water mixtures can be predicted from the proposed correlations provided the critical quality (or superficial gas Reynolds number) and the critical pressure gradient for transition from bubble/plug-to-slug flow are known. A comparison of the proposed method with that of Lockhart and Martinelli is presented and discussed.
    keyword(s): Pressure drop , Water , Flow (Dynamics) , Reynolds number , Bubbles , Mixtures , Pressure gradient AND Slug ,
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      Correlation of Adiabatic Two-Phase Pressure Drop Data Using the Frictional Law of Corresponding States

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/112158
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    • Journal of Fluids Engineering

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    contributor authorN. T. Obot
    contributor authorM. W. Wambsganss
    contributor authorD. M. France
    contributor authorJ. A. Jendrzejczyk
    date accessioned2017-05-08T23:41:43Z
    date available2017-05-08T23:41:43Z
    date copyrightJune, 1993
    date issued1993
    identifier issn0098-2202
    identifier otherJFEGA4-27076#317_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/112158
    description abstractA method, based on that developed for single-phase flow, is proposed for the correlation of two-phase frictional pressure drop data. It is validated using air-water data obtained on small horizontal passages of rectangular and circular cross-section for values of total mass flux G in the 50-2000 kg/m2 s range. The pressure drop for air-water mixtures can be predicted from the proposed correlations provided the critical quality (or superficial gas Reynolds number) and the critical pressure gradient for transition from bubble/plug-to-slug flow are known. A comparison of the proposed method with that of Lockhart and Martinelli is presented and discussed.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleCorrelation of Adiabatic Two-Phase Pressure Drop Data Using the Frictional Law of Corresponding States
    typeJournal Paper
    journal volume115
    journal issue2
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.2910141
    journal fristpage317
    journal lastpage323
    identifier eissn1528-901X
    keywordsPressure drop
    keywordsWater
    keywordsFlow (Dynamics)
    keywordsReynolds number
    keywordsBubbles
    keywordsMixtures
    keywordsPressure gradient AND Slug
    treeJournal of Fluids Engineering:;1993:;volume( 115 ):;issue: 002
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
    نرم افزار کتابخانه دیجیتال "دی اسپیس" فارسی شده توسط یابش برای کتابخانه های ایرانی | تماس با یابش
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