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    An Experimental and Numerical Study of Turbulent Swirling Pipe Flows

    Source: Journal of Fluids Engineering:;1998:;volume( 120 ):;issue: 001::page 54
    Author:
    R. R. Parchen
    ,
    W. Steenbergen
    DOI: 10.1115/1.2819661
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Both experimental and numerical studies have been performed aimed at the description of the decay of swirl in turbulent pipe flows. Emphasis is put on the effect of the initial velocity distribution on the rate of decay. The experiments show that, even far downstream of the swirl generator, the decay of the integral amount of angular momentum depends on the initial velocity distribution. This suggests that the description of the decay in terms of the widely suggested single exponential, function, is not sufficient. The calculations are based on (i) a standard k – ε model and (ii) models based on an algebraic transport model for the turbulent stresses. It appears that in a weakly swirling pipe flow, second-order models reduce to simple modifications of the standard k – ε model. While the standard k – ε model predicts a decay largely insensitive to the initial velocity distribution, the modified versions of the k – ε model, the ASM and the RSM, predict a strong sensitivity to the initial velocity distribution. Nevertheless, the standard k – ε model seems to predict the rate of decay of the swirl better than the second-order models. It is concluded that the corrections for the streamline curvature introduced by the second-order closures, largely overestimate the effect of rotation on the radial exchange of angular momentum.
    keyword(s): Turbulence , Pipe flow , Swirling flow , Angular momentum , Rotation , Stress AND Generators ,
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      An Experimental and Numerical Study of Turbulent Swirling Pipe Flows

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    contributor authorR. R. Parchen
    contributor authorW. Steenbergen
    date accessioned2017-05-08T23:57:01Z
    date available2017-05-08T23:57:01Z
    date copyrightMarch, 1998
    date issued1998
    identifier issn0098-2202
    identifier otherJFEGA4-27126#54_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/120673
    description abstractBoth experimental and numerical studies have been performed aimed at the description of the decay of swirl in turbulent pipe flows. Emphasis is put on the effect of the initial velocity distribution on the rate of decay. The experiments show that, even far downstream of the swirl generator, the decay of the integral amount of angular momentum depends on the initial velocity distribution. This suggests that the description of the decay in terms of the widely suggested single exponential, function, is not sufficient. The calculations are based on (i) a standard k – ε model and (ii) models based on an algebraic transport model for the turbulent stresses. It appears that in a weakly swirling pipe flow, second-order models reduce to simple modifications of the standard k – ε model. While the standard k – ε model predicts a decay largely insensitive to the initial velocity distribution, the modified versions of the k – ε model, the ASM and the RSM, predict a strong sensitivity to the initial velocity distribution. Nevertheless, the standard k – ε model seems to predict the rate of decay of the swirl better than the second-order models. It is concluded that the corrections for the streamline curvature introduced by the second-order closures, largely overestimate the effect of rotation on the radial exchange of angular momentum.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleAn Experimental and Numerical Study of Turbulent Swirling Pipe Flows
    typeJournal Paper
    journal volume120
    journal issue1
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.2819661
    journal fristpage54
    journal lastpage61
    identifier eissn1528-901X
    keywordsTurbulence
    keywordsPipe flow
    keywordsSwirling flow
    keywordsAngular momentum
    keywordsRotation
    keywordsStress AND Generators
    treeJournal of Fluids Engineering:;1998:;volume( 120 ):;issue: 001
    contenttypeFulltext
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