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    Experimental and Numerical Development of a Two-Phase Venturi Flow Meter

    Source: Journal of Fluids Engineering:;2004:;volume( 126 ):;issue: 003::page 457
    Author:
    Euge⁁nio S. Rosa
    ,
    Rigoberto E. M. Morales
    DOI: 10.1115/1.1758267
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: An algebraic model is developed access the gas and the liquid flow rates of a two-phase mixture through a Venturi tube. The flow meter operates with upward bubbly flows with low gas content, i.e., volumetric void fraction bellow 12%. The algebraic model parameters stem from numerical modeling and its output is checked against the experimental values. An indoor test facility operating with air-water and air-glycerin mixtures in a broad range of gas and liquid flow rates reproduces the upward bubbly flow through the Venturi tube. Measurements of gas and liquid flow rates plus the static pressure acroos the Venturi constitute the experimental database. The numerical flow modeling uses the isothermal, axis-symmetric with no phase change representation of the Two-Fluid model. The numerical output feeds the Venturi’s algebraic model with the proper constants and parameters embodying the two-phase flow physics. The novelty of this approach is the development of each flow meter model accordingly to its on characteristics. The flow predictions deviates less than 14% from experimental data while the mixture pipe Reynolds number spanned from 500 to 50,000.
    keyword(s): Pressure , Flow (Dynamics) , Fluids , Mixtures , Venturi tubes , Flowmeters , Equations , Porosity , Pipes , Databases , Bubbly flow , Computer simulation , Turbulence , Uncertainty AND Water ,
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      Experimental and Numerical Development of a Two-Phase Venturi Flow Meter

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    https://yetl.yabesh.ir/yetl1/handle/yetl/130252
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    contributor authorEuge⁁nio S. Rosa
    contributor authorRigoberto E. M. Morales
    date accessioned2017-05-09T00:13:27Z
    date available2017-05-09T00:13:27Z
    date copyrightMay, 2004
    date issued2004
    identifier issn0098-2202
    identifier otherJFEGA4-27197#457_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/130252
    description abstractAn algebraic model is developed access the gas and the liquid flow rates of a two-phase mixture through a Venturi tube. The flow meter operates with upward bubbly flows with low gas content, i.e., volumetric void fraction bellow 12%. The algebraic model parameters stem from numerical modeling and its output is checked against the experimental values. An indoor test facility operating with air-water and air-glycerin mixtures in a broad range of gas and liquid flow rates reproduces the upward bubbly flow through the Venturi tube. Measurements of gas and liquid flow rates plus the static pressure acroos the Venturi constitute the experimental database. The numerical flow modeling uses the isothermal, axis-symmetric with no phase change representation of the Two-Fluid model. The numerical output feeds the Venturi’s algebraic model with the proper constants and parameters embodying the two-phase flow physics. The novelty of this approach is the development of each flow meter model accordingly to its on characteristics. The flow predictions deviates less than 14% from experimental data while the mixture pipe Reynolds number spanned from 500 to 50,000.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleExperimental and Numerical Development of a Two-Phase Venturi Flow Meter
    typeJournal Paper
    journal volume126
    journal issue3
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.1758267
    journal fristpage457
    journal lastpage467
    identifier eissn1528-901X
    keywordsPressure
    keywordsFlow (Dynamics)
    keywordsFluids
    keywordsMixtures
    keywordsVenturi tubes
    keywordsFlowmeters
    keywordsEquations
    keywordsPorosity
    keywordsPipes
    keywordsDatabases
    keywordsBubbly flow
    keywordsComputer simulation
    keywordsTurbulence
    keywordsUncertainty AND Water
    treeJournal of Fluids Engineering:;2004:;volume( 126 ):;issue: 003
    contenttypeFulltext
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