Thermal Entry for Low Reynolds Number Turbulent FlowSource: Journal of Fluids Engineering:;1969:;volume( 091 ):;issue: 001::page 87DOI: 10.1115/1.3571033Publisher: The American Society of Mechanical Engineers (ASME)
Abstract: The thermal entrance problem for low Reynolds number, turbulent flow of gases in circular tubes is solved analytically by the method of Sparrow, Hallman, and Siegel. Fluid properties are considered constant. The solution is based on a Reynolds-number-dependent velocity profile developed, in a companion paper, by modifying Reichardt’s wall and middle law eddy diffusivity expressions. Tabular values of the eigenvalues and normalized Nusselt numbers are presented for a range of Reynolds numbers from 3,000 to 50,000. The axial variation of Nusselt number is found to be correlated by NuNu∞ = 1 + 0.8(1+70,000 Re−3/2) xD−1 to within ±5 percent for x/D ≥ 2. The fully developed value agrees with the Dittus-Boelter correlation. For the eigenvalues, λn 2 , and the associated constants, An , correlations of the form λn2 = a1,n Re−b1,n + c1,n Re−d1,nAn = a2,n Re−b2,n + c2,nRe−d2,n are obtained. Heat transfer data are presented, primarily for helium, for the conditions of the analysis. In the low Reynolds number turbulent regime, these data clearly support the present analytical solution.
keyword(s): Turbulence , Reynolds number , Eigenvalues , Helium , Eddies (Fluid dynamics) , Heat transfer , Fluids AND Gases ,
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contributor author | H. C. Reynolds | |
contributor author | T. B. Swearingen | |
contributor author | D. M. McEligot | |
date accessioned | 2017-05-09T00:22:43Z | |
date available | 2017-05-09T00:22:43Z | |
date copyright | March, 1969 | |
date issued | 1969 | |
identifier issn | 0098-2202 | |
identifier other | JFEGA4-27327#87_1.pdf | |
identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/135223 | |
description abstract | The thermal entrance problem for low Reynolds number, turbulent flow of gases in circular tubes is solved analytically by the method of Sparrow, Hallman, and Siegel. Fluid properties are considered constant. The solution is based on a Reynolds-number-dependent velocity profile developed, in a companion paper, by modifying Reichardt’s wall and middle law eddy diffusivity expressions. Tabular values of the eigenvalues and normalized Nusselt numbers are presented for a range of Reynolds numbers from 3,000 to 50,000. The axial variation of Nusselt number is found to be correlated by NuNu∞ = 1 + 0.8(1+70,000 Re−3/2) xD−1 to within ±5 percent for x/D ≥ 2. The fully developed value agrees with the Dittus-Boelter correlation. For the eigenvalues, λn 2 , and the associated constants, An , correlations of the form λn2 = a1,n Re−b1,n + c1,n Re−d1,nAn = a2,n Re−b2,n + c2,nRe−d2,n are obtained. Heat transfer data are presented, primarily for helium, for the conditions of the analysis. In the low Reynolds number turbulent regime, these data clearly support the present analytical solution. | |
publisher | The American Society of Mechanical Engineers (ASME) | |
title | Thermal Entry for Low Reynolds Number Turbulent Flow | |
type | Journal Paper | |
journal volume | 91 | |
journal issue | 1 | |
journal title | Journal of Fluids Engineering | |
identifier doi | 10.1115/1.3571033 | |
journal fristpage | 87 | |
journal lastpage | 94 | |
identifier eissn | 1528-901X | |
keywords | Turbulence | |
keywords | Reynolds number | |
keywords | Eigenvalues | |
keywords | Helium | |
keywords | Eddies (Fluid dynamics) | |
keywords | Heat transfer | |
keywords | Fluids AND Gases | |
tree | Journal of Fluids Engineering:;1969:;volume( 091 ):;issue: 001 | |
contenttype | Fulltext |