Turbulent energy production peak and its location from inner most log law or power law velocity in a turbulent channel/pipe and Couette flows

被引:4
作者
Afzal, Noor [1 ]
Seena, Abu [2 ]
Bushra, A. [3 ]
机构
[1] 5526 Green Oak Dr, San Jose, CA 96129 USA
[2] Samsung C&T, Tower 2,145 Pangyoyeok Ro, Seongnam Si 13530, Gyeonggi Do, South Korea
[3] Appl Mat Inc, 3330 Scott Blvd, Santa Clara, CA 95054 USA
关键词
DIRECT NUMERICAL-SIMULATION; PIPE; STATISTICS; LAYER;
D O I
10.1016/j.euromechflu.2017.08.013
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
The present work deals with the inner most, log law velocity and inner most power law velocity, and the associated Reynolds shear stresses, for turbulent energy production in the buffer layer of a fully developed turbulent channel or pipe and Couette flow. The Reynolds momentum equations have been are analyzed with out any closure model of eddy viscosity, mixing length etc. The equivalence of power law solutions with log law solution is demonstrated for large Reynolds numbers. Turbulent energy production asymptotic theory is presented. In a fully developed turbulent channel/pipe flow the theory shows that the peak of production and its location are universal numbers for large friction Reynolds numbers, but for lower Reynolds number theory show dependence on inverse of friction Reynolds number R-tau(-1). For turbulent Couette flow peak of production and its location are universal numbers for all friction Reynolds numbers. The turbulent energy production theory predictions in the buffer layer are compared with experimental and DNS data which support the predictions, that in channel or pipe the prediction depend on friction Reynolds number dependence like R-tau(-1) and for Couette flow the predictions are universal numbers. (C) 2017 Elsevier Masson SAS. All rights reserved.
引用
收藏
页码:178 / 184
页数:7
相关论文
共 34 条
[1]   Surface heat-flux fluctuations in a turbulent channel flow up to Reτ=1020 with Pr=0.025 and 0.71 [J].
Abe, H ;
Kawamura, H ;
Matsuo, Y .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2004, 25 (03) :404-419
[2]  
AFZAL N, 1976, J FLUID MECH, V74, P113, DOI 10.1017/S0022112076001717
[3]   ASYMPTOTIC ANALYSIS OF TURBULENT COUETTE-FLOW [J].
AFZAL, N .
FLUID DYNAMICS RESEARCH, 1993, 12 (03) :163-171
[4]   MESOLAYER THEORY FOR TURBULENT FLOWS [J].
AFZAL, N .
AIAA JOURNAL, 1984, 22 (03) :437-439
[5]   FULLY-DEVELOPED TURBULENT-FLOW IN A PIPE - AN INTERMEDIATE LAYER [J].
AFZAL, N .
INGENIEUR ARCHIV, 1982, 52 (06) :355-377
[6]   MILLIKANS ARGUMENT AT MODERATELY LARGE REYNOLDS-NUMBER [J].
AFZAL, N .
PHYSICS OF FLUIDS, 1976, 19 (04) :600-602
[7]   Power law and log law velocity profiles in fully developed turbulent pipe flow: equivalent relations at large Reynolds numbers [J].
Afzal, N .
ACTA MECHANICA, 2001, 151 (3-4) :171-183
[8]  
AFZAL N, 1997, P 7 AS C FLUID MECH, P805
[9]  
Afzal N., 2005, 43 AIAA AER SCI M EX, P12
[10]  
Afzal N., 2009, IISC CENT INT C AER, P137