%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %%%%%% %%%%%% %%%%%% Turbulent Pouiseille Channel Flow %%%%%% %%%%%% with Heat Transfer %%%%%% %%%%%% %%%%%% %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %%%%%% %%%%%% %%%%%% Supported by %%%%%% %%%%%% MINECO/FEDER, ENE2015-71333-R %%%%%% %%%%%% MINECO/FEDER, RTI2018-102256-B-I00 %%%%%% %%%%%% GVA/FEDER project ACIF2018. %%%%%% %%%%%% %%%%%% %%%%%% %%%%%% %%%%%% 2016 - 2021 %%%%%% %%%%%% %%%%%% %%%%%% %%%%%% %%%%%% Chair of Aerospace Engineering %%%%%% %%%%%% IUMPA %%%%%% %%%%%% %%%%%% %%%%%% Universitat Politecnica de Valencia, %%%%%% %%%%%% Camino de Vera, s/n 46022 Valencia, Spain %%%%%% %%%%%% %%%%%% %%%%%% Contact: sergio.hoyas@mot.upv.es %%%%%% %%%%%% Contact: fraalvi@alumni.upv.es %%%%%% %%%%%% %%%%%% %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %%%%%% %%%%%% %%%%%% <<< CAUTION >>> %%%%%% %%%%%% %%%%%% %%%%%% All rights are reserved by the authors. %%%%%% %%%%%% No part of the data described herein may be represented %%%%%% %%%%%% without reference. The data base may be used without %%%%%% %%%%%% notification to the author's laboratory, asuming that %%%%%% %%%%%% it has been properly cited. %%%%%% %%%%%% %%%%%% %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %% %% %% REFERENCES: %% %% %% %% - Method: %% %% %% %% Lluesma-Rodriguez, F., Alcantara-Avila, F., Perez-Quiles, M.J., %% %% Hoyas S. %% %% A Code for Simulating Heat Transfer in Turbulent Channel Flow %% %% Mathematics 2021, 9(7), 756; %% %% ------------------------------------------------------------ %% %% %% %% - Data & discussion: %% %% %% %% Alcantara-Avila, F., Hoyas, S., Perez-Quiles, M.J. %% %% Direct Numerical Simulation of thermal channel flow for %% %% Re_\tau = 5000 and Pr = 0.71. %% %% Journal of Fluid Mechanics, 2021, Vol916, 10 June 2021 , A29. %% %% ------------------------------------------------------------ %% %% Alcantara-Avila, F., Hoyas, S. %% %% Direct numerical simulation of thermal channel flow for %% %% medium-high Prandtl numbers up to Re_\tau=2000, %% %% International Journal of Heat and Mass Transfer, 176, 2021 %% %% ------------------------------------------------------------ %% %% Alcantara-Avila, F., Hoyas, S., Perez-Quiles, M.J. %% %% DNS of thermal channel flow up to Re\_tau =2000 for medium to %% %% low Prandtl numbers %% %% IJHMT, 2018, 127, pp. 349-361 %% %% ------------------------------------------------------------ %% %% Lluesma-Rodriguez, F., Hoyas, S., Perez-Quiles, M.J. %% %% Influence of the computational domain on DNS of turbulent heat %% %% transfer up to Re_\tau=2000 for Pr=0.71 %% %% IJHMT, 122, pp. 983-992 %% %% %% %% NOMENCLATURE: %% %% x = streamwise coordinate %% %% y = wall-normal coordinate %% %% z = spanwise coordinate %% %% h = channel half-width %% %% U = mean streamwise velocity %% %% Th = thermal field %% %% utau = friction velocity %% %% Ttau = friction temperature %% %% nu = kinematic viscosity %% %% Retau = Reynolds number utau*h/nu %% %% Pr = Prandtl number %% %% Nu = Nusselt number %% %% theta' = rms values of temperatures fluctuations %% %% th'*u', th'*v' = Thermal fluxes %% %% (.)+ = normalized by utau, Ttau and nu %% %% %% %% %% %% BOX SIZE in h (x,y,z): 2pi|2|1pi %% %% FLOW CONDITIONS: Retau = 497 (Re = 10200), Pr=0.0200 %% %% utau = 0.048732 %% %% Ttau = 0.999841 %% %% Nu = 7.065982 %% %% %% %% Data file created: April 06, 2018 %% %% %% %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% % y/h y+ U+ Th+ u' v' w' th'+ u'v'+ th'u'+ th'v'+ dU+/dy+ dTh+/dy+ 0.00000000 0.00000000 0.00000000 0.00000000 0.00000000 0.00000000 0.00000000 0.00000000 0.00000000 0.00000000 0.00000000 1.00049356 0.02000009 0.00145533 0.72340061 0.72316410 0.01446793 0.28846383 0.00554299 0.17008481 0.00383319 -0.00038541 0.00030923 -0.00000367 0.99865842 0.01999945 0.00312698 1.55432736 1.55115194 0.03108504 0.61531216 0.02249072 0.33280142 0.00823734 -0.00394897 0.00151305 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