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contributor authorF. Durst
contributor authorS. Ray
contributor authorB. Ünsal
contributor authorO. A. Bayoumi
date accessioned2017-05-09T00:16:25Z
date available2017-05-09T00:16:25Z
date copyrightNovember, 2005
date issued2005
identifier issn0098-2202
identifier otherJFEGA4-27213#1154_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/131930
description abstractThe authors’ research work into fully developed pulsating and oscillating laminar pipe and channel flows raised questions regarding the development length of the corresponding steady flow. For this development length, i.e., the distance from the entrance of the pipe to the axial position where the flow reaches the parabolic velocity profile of the Hagen-Poiseuille flow, a wide range of contradictory data exists. This is shown through a short review of the existing literature. Superimposed diffusion and convection, together with order of magnitude considerations, suggest that the normalized development length can be expressed as L∕D=C0+C1Re and for Re→0 one obtains C0=0.619, whereas for Re→∞ one obtains C1=0.0567. This relationship is given only once in the literature and it is presumed to be valid for all Reynolds numbers. Numerical studies show that it is only valid for Re→0 and Re→∞. The development length of laminar, plane channel flow was also investigated. The authors obtained similar results to those for the pipe flow: L∕D=C0′+C1′; Re, where C0′=0.631 and C1′=0.044. Finally, correlations are given to express L∕D analytically for the entire Re range for both laminar pipe and channel flows.
publisherThe American Society of Mechanical Engineers (ASME)
titleThe Development Lengths of Laminar Pipe and Channel Flows
typeJournal Paper
journal volume127
journal issue6
journal titleJournal of Fluids Engineering
identifier doi10.1115/1.2063088
journal fristpage1154
journal lastpage1160
identifier eissn1528-901X
keywordsDiffusion (Physics)
keywordsReynolds number
keywordsChannel flow
keywordsPipe flow
keywordsPipes
keywordsEquations
keywordsFlow (Dynamics) AND Convection
treeJournal of Fluids Engineering:;2005:;volume( 127 ):;issue: 006
contenttypeFulltext


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