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    The Prediction of Swirl and Inlet Turbulence Kinetic Energy Effects on Confined Jet Mixing

    Source: Journal of Fluids Engineering:;1975:;volume( 097 ):;issue: 001::page 51
    Author:
    C. J. Hendricks
    ,
    J. A. Brighton
    DOI: 10.1115/1.3447215
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Mixing of a turbulent jet with a coaxial slower-moving secondary stream in a constant diameter tube was investigated. Of special interests were the effects of swirling the jet and initial turbulence kinetic energy. The analysis involved a numerical solution of the governing flow equations which were simplified by the Prandtl boundary layer assumptions. The two unknown turbulent stresses in the flow equations were modeled by defining an isotropic effective viscosity. The effective viscosity was calculated from a two-equation model of turbulence. The turbulence model was modified for swirling flows. Predicted results were compared with experimental results of several investigators. Good agreement was obtained when calculated results were compared with mean velocity and wall pressure data. The addition of swirl to the jet increased the rate of spread of the jet and resulted in decreasing the axial length required for mixing. The initial turbulence levels of the streams were found to have a significant effect on the distribution of mean velocity and pressure. This dependence has not been considered by most investigators and makes it imperative that experimentalists include turbulence information in their presentation of results.
    keyword(s): Turbulence , Kinetic energy , Equations , Swirling flow , Viscosity , Pressure , Flow (Dynamics) , Stress AND Boundary layers ,
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      The Prediction of Swirl and Inlet Turbulence Kinetic Energy Effects on Confined Jet Mixing

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    http://yetl.yabesh.ir/yetl1/handle/yetl/87692
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    contributor authorC. J. Hendricks
    contributor authorJ. A. Brighton
    date accessioned2017-05-08T22:59:01Z
    date available2017-05-08T22:59:01Z
    date copyrightMarch, 1975
    date issued1975
    identifier issn0098-2202
    identifier otherJFEGA4-26866#51_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/87692
    description abstractMixing of a turbulent jet with a coaxial slower-moving secondary stream in a constant diameter tube was investigated. Of special interests were the effects of swirling the jet and initial turbulence kinetic energy. The analysis involved a numerical solution of the governing flow equations which were simplified by the Prandtl boundary layer assumptions. The two unknown turbulent stresses in the flow equations were modeled by defining an isotropic effective viscosity. The effective viscosity was calculated from a two-equation model of turbulence. The turbulence model was modified for swirling flows. Predicted results were compared with experimental results of several investigators. Good agreement was obtained when calculated results were compared with mean velocity and wall pressure data. The addition of swirl to the jet increased the rate of spread of the jet and resulted in decreasing the axial length required for mixing. The initial turbulence levels of the streams were found to have a significant effect on the distribution of mean velocity and pressure. This dependence has not been considered by most investigators and makes it imperative that experimentalists include turbulence information in their presentation of results.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleThe Prediction of Swirl and Inlet Turbulence Kinetic Energy Effects on Confined Jet Mixing
    typeJournal Paper
    journal volume97
    journal issue1
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.3447215
    journal fristpage51
    journal lastpage59
    identifier eissn1528-901X
    keywordsTurbulence
    keywordsKinetic energy
    keywordsEquations
    keywordsSwirling flow
    keywordsViscosity
    keywordsPressure
    keywordsFlow (Dynamics)
    keywordsStress AND Boundary layers
    treeJournal of Fluids Engineering:;1975:;volume( 097 ):;issue: 001
    contenttypeFulltext
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