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    Erratum: “Flow Regimes for Laminar Film Condensation on a Vertical Plate With an Upward Vapor Flow” [ASME J. Heat Transfer, 142, pp. 041603-1–041603-9 (2020); DOI: 10.1115/1.4046307]

    Source: Journal of Heat Transfer:;2021:;volume( 143 ):;issue: 007::page 077001-1
    Author:
    Kanatani, Kentaro
    DOI: 10.1115/1.4050994
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: The expression for the boundary condition of the solution types (ii) and (iii) at the bottom (z = 0), Eq. (27) in the original paper, is incorrect. The correct version is (1)V0=−duδdx(ζ−ζ2Δ+ζ33Δ2−Δ3)−(U∞−uδ)[(−1+2ζΔ−ζ2Δ2)dζdx+(13−ζ2Δ2+2ζ33Δ3)dΔdx]Accordingly, Eq. (29) in the original paper is changed to (2)(w−η)[14−7w+3w2+(11−w)η−10H(w+η)(1+η)+4(1−w)3R2(w+η)]=ρ[4(1+w+3w2)+2(1+9w)η−152R2(w+η)2{1−w+ηH(1−w)}]where η=h2/2. Actually, there are multiple solution branches of w and η satisfying Eq. (2). Among them, the physically realistic solutions are those with (i) a zero or negative flow rate, and (ii) a positive thickness of the vapor boundary layer, which is represented by (3)−η<w≤η3(see Eqs. (9) and (22) in the original paper).
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      Erratum: “Flow Regimes for Laminar Film Condensation on a Vertical Plate With an Upward Vapor Flow” [ASME J. Heat Transfer, 142, pp. 041603-1–041603-9 (2020); DOI: 10.1115/1.4046307]

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    http://yetl.yabesh.ir/yetl1/handle/yetl/4278289
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    contributor authorKanatani, Kentaro
    date accessioned2022-02-06T05:33:49Z
    date available2022-02-06T05:33:49Z
    date copyright5/17/2021 12:00:00 AM
    date issued2021
    identifier issn0022-1481
    identifier otherht_143_07_077001.pdf
    identifier urihttp://yetl.yabesh.ir/yetl1/handle/yetl/4278289
    description abstractThe expression for the boundary condition of the solution types (ii) and (iii) at the bottom (z = 0), Eq. (27) in the original paper, is incorrect. The correct version is (1)V0=−duδdx(ζ−ζ2Δ+ζ33Δ2−Δ3)−(U∞−uδ)[(−1+2ζΔ−ζ2Δ2)dζdx+(13−ζ2Δ2+2ζ33Δ3)dΔdx]Accordingly, Eq. (29) in the original paper is changed to (2)(w−η)[14−7w+3w2+(11−w)η−10H(w+η)(1+η)+4(1−w)3R2(w+η)]=ρ[4(1+w+3w2)+2(1+9w)η−152R2(w+η)2{1−w+ηH(1−w)}]where η=h2/2. Actually, there are multiple solution branches of w and η satisfying Eq. (2). Among them, the physically realistic solutions are those with (i) a zero or negative flow rate, and (ii) a positive thickness of the vapor boundary layer, which is represented by (3)−η<w≤η3(see Eqs. (9) and (22) in the original paper).
    publisherThe American Society of Mechanical Engineers (ASME)
    titleErratum: “Flow Regimes for Laminar Film Condensation on a Vertical Plate With an Upward Vapor Flow” [ASME J. Heat Transfer, 142, pp. 041603-1–041603-9 (2020); DOI: 10.1115/1.4046307]
    typeJournal Paper
    journal volume143
    journal issue7
    journal titleJournal of Heat Transfer
    identifier doi10.1115/1.4050994
    journal fristpage077001-1
    journal lastpage077001-2
    page2
    treeJournal of Heat Transfer:;2021:;volume( 143 ):;issue: 007
    contenttypeFulltext
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    DSpace software copyright © 2002-2015  DuraSpace
    نرم افزار کتابخانه دیجیتال "دی اسپیس" فارسی شده توسط یابش برای کتابخانه های ایرانی | تماس با یابش
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