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    Thin-Film Flow at Moderate Reynolds Number

    Source: Journal of Fluids Engineering:;2000:;volume( 122 ):;issue: 004::page 774
    Author:
    Kenneth J. Ruschak
    ,
    Senior Research Associate
    ,
    Steven J. Weinstein
    ,
    Research Associate
    DOI: 10.1115/1.1319499
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: Viscous, laminar, gravitationally-driven flow of a thin film over a round-crested weir is analyzed for moderate Reynolds numbers. A previous analysis of this flow utilized a momentum integral approach with a semiparabolic velocity profile to obtain an equation for the film thickness (Ruschak, K. J., and Weinstein, S. J., 1999, “Viscous Thin-Film Flow Over a Round-Crested Weir,” ASME J. Fluids Eng., 121 , pp. 673–677). In this work, a viscous boundary layer is introduced in the manner of Haugen (Haugen, R., 1968, “Laminar Flow Around a Vertical Wall,” ASME J. Appl. Mech. 35 , pp. 631–633). As in the previous analysis of Ruschak and Weinstein, the approximate equations have a critical point that provides an internal boundary condition for a bounded solution. The complication of a boundary layer is found to have little effect on the thickness profile while introducing a weak singularity at its beginning. The thickness of the boundary layer grows rapidly, and there is little cumulative effect of the increased wall friction. Regardless of whether a boundary layer is incorporated, the approximate free-surface profiles are close to profiles from finite-element solutions of the Navier-Stokes equation. Similar results are obtained for the related problem of developing flow on a vertical wall (Cerro, R. L., and Whitaker, S., 1971, “Entrance Region Flows With a Free Surface: the Falling Liquid Film,” Chem. Eng. Sci., 26 , pp. 785–798). Less accurate results are obtained for decelerating flow on a horizontal wall (Watson, E. J., 1964, “The Radial Spread of a Liquid Jet Over a Horizontal Plane,” J. Fluid Mech. 20 , pp. 481–499) where the flow is not gravitationally driven. [S0098-2202(00)01904-0]
    keyword(s): Flow (Dynamics) , Reynolds number , Navier-Stokes equations , Boundary layers , Equations , Film thickness , Thin films AND Thickness ,
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      Thin-Film Flow at Moderate Reynolds Number

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    contributor authorKenneth J. Ruschak
    contributor authorSenior Research Associate
    contributor authorSteven J. Weinstein
    contributor authorResearch Associate
    date accessioned2017-05-09T00:02:37Z
    date available2017-05-09T00:02:37Z
    date copyrightDecember, 2000
    date issued2000
    identifier issn0098-2202
    identifier otherJFEGA4-27157#774_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/123830
    description abstractViscous, laminar, gravitationally-driven flow of a thin film over a round-crested weir is analyzed for moderate Reynolds numbers. A previous analysis of this flow utilized a momentum integral approach with a semiparabolic velocity profile to obtain an equation for the film thickness (Ruschak, K. J., and Weinstein, S. J., 1999, “Viscous Thin-Film Flow Over a Round-Crested Weir,” ASME J. Fluids Eng., 121 , pp. 673–677). In this work, a viscous boundary layer is introduced in the manner of Haugen (Haugen, R., 1968, “Laminar Flow Around a Vertical Wall,” ASME J. Appl. Mech. 35 , pp. 631–633). As in the previous analysis of Ruschak and Weinstein, the approximate equations have a critical point that provides an internal boundary condition for a bounded solution. The complication of a boundary layer is found to have little effect on the thickness profile while introducing a weak singularity at its beginning. The thickness of the boundary layer grows rapidly, and there is little cumulative effect of the increased wall friction. Regardless of whether a boundary layer is incorporated, the approximate free-surface profiles are close to profiles from finite-element solutions of the Navier-Stokes equation. Similar results are obtained for the related problem of developing flow on a vertical wall (Cerro, R. L., and Whitaker, S., 1971, “Entrance Region Flows With a Free Surface: the Falling Liquid Film,” Chem. Eng. Sci., 26 , pp. 785–798). Less accurate results are obtained for decelerating flow on a horizontal wall (Watson, E. J., 1964, “The Radial Spread of a Liquid Jet Over a Horizontal Plane,” J. Fluid Mech. 20 , pp. 481–499) where the flow is not gravitationally driven. [S0098-2202(00)01904-0]
    publisherThe American Society of Mechanical Engineers (ASME)
    titleThin-Film Flow at Moderate Reynolds Number
    typeJournal Paper
    journal volume122
    journal issue4
    journal titleJournal of Fluids Engineering
    identifier doi10.1115/1.1319499
    journal fristpage774
    journal lastpage778
    identifier eissn1528-901X
    keywordsFlow (Dynamics)
    keywordsReynolds number
    keywordsNavier-Stokes equations
    keywordsBoundary layers
    keywordsEquations
    keywordsFilm thickness
    keywordsThin films AND Thickness
    treeJournal of Fluids Engineering:;2000:;volume( 122 ):;issue: 004
    contenttypeFulltext
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