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    Liquid Taylor Bubbles Rising in a Vertical Column of a Heavier Liquid: An Approximate Analysis

    Source: Journal of Fluids Engineering:;2009:;volume( 131 ):;issue: 001::page 11303
    Author:
    T. K. Mandal
    ,
    G. Das
    ,
    P. K. Das
    DOI: 10.1115/1.3026730
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: It has been noted that a volume of lighter liquid when injected into a stationary column of a heavier liquid, it rises up as a simple elongated Taylor bubble. In the present study, experimental and theoretical analyses have been performed to understand the rise of liquid Taylor bubbles. The experiments have been performed with different liquid pairs with their viscosities ranging from 0.71mPas to 1.75mPas and conduit sizes ranging from 0.012 m to 0.0461 m. The bubble shape has been predicted using a potential flow analysis and validated from photographic measurements. This analysis has been further modified to predict the rise velocity. The modified analysis accounts for the density difference between the two liquids, viscosity effects of the primary liquid, and interfacial tension of two fluids. A semi-empirical equation has been developed, which gives satisfactory results for most of the cases.
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      Liquid Taylor Bubbles Rising in a Vertical Column of a Heavier Liquid: An Approximate Analysis

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    http://yetl.yabesh.ir/yetl1/handle/yetl/140801
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    contributor authorT. K. Mandal
    contributor authorG. Das
    contributor authorP. K. Das
    date accessioned2017-05-09T00:33:19Z
    date available2017-05-09T00:33:19Z
    date copyrightJanuary, 2009
    date issued2009
    identifier issn0098-2202
    identifier otherJFEGA4-27354#011303_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/140801
    description abstractIt has been noted that a volume of lighter liquid when injected into a stationary column of a heavier liquid, it rises up as a simple elongated Taylor bubble. In the present study, experimental and theoretical analyses have been performed to understand the rise of liquid Taylor bubbles. The experiments have been performed with different liquid pairs with their viscosities ranging from 0.71mPas to 1.75mPas and conduit sizes ranging from 0.012 m to 0.0461 m. The bubble shape has been predicted using a potential flow analysis and validated from photographic measurements. This analysis has been further modified to predict the rise velocity. The modified analysis accounts for the density difference between the two liquids, viscosity effects of the primary liquid, and interfacial tension of two fluids. A semi-empirical equation has been developed, which gives satisfactory results for most of the cases.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleLiquid Taylor Bubbles Rising in a Vertical Column of a Heavier Liquid: An Approximate Analysis
    typeJournal Paper
    journal volume131
    journal issue1
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.3026730
    journal fristpage11303
    identifier eissn1528-901X
    treeJournal of Fluids Engineering:;2009:;volume( 131 ):;issue: 001
    contenttypeFulltext
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