1952
DOI: 10.2514/8.2381
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Simplified Laminar Boundary-Layer Calculations for Bodies of Revolution and Yawed Wings

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Cited by 59 publications
(4 citation statements)
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“…The value of 8 , is a function of the particular headform and the wetted surface velocity distribution. Using the pressure distributions given by Brennen ( 1968) for the wetted surface of a cavitating sphere and the approximate integral method of Rott & Crabtree (1952) 8, was found to be given by I,/(Ru/U) (R and v being the radius of the sphere and the kinematic viscosity) where I was estimated as 0.3, varying negligibly with cavitation number within the range 0 < r < 0.4.…”
Section: MI = 2tt(cmmentioning
confidence: 99%
“…The value of 8 , is a function of the particular headform and the wetted surface velocity distribution. Using the pressure distributions given by Brennen ( 1968) for the wetted surface of a cavitating sphere and the approximate integral method of Rott & Crabtree (1952) 8, was found to be given by I,/(Ru/U) (R and v being the radius of the sphere and the kinematic viscosity) where I was estimated as 0.3, varying negligibly with cavitation number within the range 0 < r < 0.4.…”
Section: MI = 2tt(cmmentioning
confidence: 99%
“…A crude estimate of this constant can be obtained either by reducing the axisymmetrical problem to a Falkner-Skan flow using Mangler's transformation and approximating to the outer flow (for example by threedimensional sink flow) or by applying-since the flow is accelerating-a simple method of the Kkm&n-Pohlhausen type, e.g. Walz's method as extended by Rott & Crabtree (1952) using the pressure distribution near the lip as computed by Frank1 for slit flow.…”
Section: The Euler Limitmentioning
confidence: 99%
“…The Reynolds number of the secondary stream was 42,000 for all four cycles; the Reynolds number of the tertiary stream ranged from 17,000 in cycle A to 25,000 in cycle D. These values are low enough to support laminar boundary layers at the exits of the secondary and tertiary streams. A compressible Thwaites method [32] was used to calculate of the boundary-layer thickness by approximating the annular secondary and tertiary ducts as twodimensional. The calculated displacement thickness of the secondary flow is 0.024 mm.…”
Section: Viscous Effectsmentioning
confidence: 99%