Solutions of equations for the thermal boundary layer at a rotating axisymmetric surface

Dorfman, L. A.; Mironova, V.A

doi:10.1016/0017-9310(70)90026-8

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Introduction1

Melting In Porous Media1

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1972

2004

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Cited by 12 publications

(2 citation statements)

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“…The results of Banks [4] which are based on series solution (in powers of meridional angle) show notably poor agreement with experimental data. Similar criticism can be made about the approximate methods of Dorfman and Serazetdinov [5] and of Dorfman and Mironova [6]. None of these studies include the buoyancy effects.…”

Section: Introductionmentioning

confidence: 88%

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The Laminar Compressible Boundary Layer on a Rotating Sphere With Heat Transfer

Hussaini

Sastry

1976

Journal of Heat Transfer

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based on the stagnant film model of a boundary layer [16], was first suggested by Spalding [10] to correct for the effect of interfacial mass transfer on diffusion in real boundary layers. This expression is also plotted in Pig. 1. While Nu/Nuo values from equation (13) do not coincide exactly with those indicated by the laminar-boundary-layer calculations, they are nevertheless comparable in form and magnitude for Pr » 1. Moreover, since it has been widely used with considerable success for mass transfer at complex surfaces submerged in laminar or turbulent flows (see, e.g., [17,18]) equation (13) is expected to correctly account for the effects of melting in many complex flow systems [4].

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Section: Introductionmentioning

confidence: 88%

“…1 (just below the curve for Pr = 10). One notes that equation (13) [5] 4.1 Dorfman and Mironova [6] 3.91 Theoretical:…”

Section: Melting In Porous Mediamentioning

confidence: 99%