On the role of roughness valleys in turbulent Rayleigh-Benard convection

被引:14
作者
Belkadi, Mebarek [1 ,2 ,3 ]
Sergent, Anne [1 ,4 ]
Fraigneau, Yann [1 ]
Podvin, Berengere [1 ]
机构
[1] Univ Paris Saclay, CNRS, LISN, F-91400 Orsay, France
[2] Sorbonne Univ, Coll Doctoral, F-75005 Paris, France
[3] Ecole Militaire Polytech, Lab Turbomachinery, Algiers 16111, Algeria
[4] Sorbonne Univ, UFR Ingengn, Fac Sci & Ingn, F-75005 Paris, France
关键词
Benard convection; turbulent convection; THERMAL-CONVECTION; HEAT-TRANSPORT; SURFACE-ROUGHNESS; ULTIMATE REGIME; NUMBER; PLATES; FLOWS; BULK;
D O I
10.1017/jfm.2021.583
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Three-dimensional direct numerical simulations are used to characterize turbulent buoyant convection in a box-shaped Rayleigh-Benard cavity with a rough bottom plate made of a series of square based blocks separated by valleys. The cavity is filled with water. The Rayleigh number varies over five decades up to . As mentioned in the literature, three successive heat transfer regimes are identified: from inactive roughness (I) to a regime (III) where the heat transfer increase is larger than that expected from only surface increase due to roughness. The heat transfers of the transitional regime II are particularly intense. After validation against experimental and numerical data from the literature, we highlight the role of the fluid retained within valleys (the inner fluid). It is shown that only the heat transfer across the fluid interface between the cavity bulk and the inner fluid is responsible for changes in the overall heat transfer at the rough plate, with an exponent of the heat transfer scaling law close to in regime II. The valley flow typifies the limits of this regime: the blocks protrude from the thermal boundary layer while remaining within the kinetic boundary layer. As compared with regimes I and III, regime II is characterized by larger temperature fluctuations, especially near the rough plate, and a larger friction coefficient. A fluctuating rough fluid layer overlaying both blocks and valleys appears in regime III, in addition to the classic boundary layers formed along the plate geometry.
引用
收藏
页数:22
相关论文
共 48 条
[31]   HIGH RAYLEIGH NUMBER CONVECTION [J].
SIGGIA, ED .
ANNUAL REVIEW OF FLUID MECHANICS, 1994, 26 :137-168
[32]   A GENERALIZATION OF MIXING-LENGTH THEORY OF TURBULENT CONVECTION [J].
SPIEGEL, EA .
ASTROPHYSICAL JOURNAL, 1963, 138 (01) :216-&
[33]   The unifying theory of scaling in thermal convection: the updated prefactors [J].
Stevens, Richard J. A. M. ;
van der Poel, Erwin P. ;
Grossmann, Siegfried ;
Lohse, Detlef .
JOURNAL OF FLUID MECHANICS, 2013, 730 :295-308
[34]   Radial boundary layer structure and Nusselt number in Rayleigh-Benard convection [J].
Stevens, Richard J. A. M. ;
Verzicco, Roberto ;
Lohse, Detlef .
JOURNAL OF FLUID MECHANICS, 2010, 643 :495-507
[35]  
Strang G., 2007, Computational Science and Engineering
[36]   Turbulent thermal convection over grooved plates [J].
Stringano, G. ;
Pascazio, G. ;
Verzicco, R. .
JOURNAL OF FLUID MECHANICS, 2006, 557 :307-336
[37]   Comparison between rough and smooth plates within the same Rayleigh-Benard cell [J].
Tisserand, J. -C. ;
Creyssels, M. ;
Gasteuil, Y. ;
Pabiou, H. ;
Gibert, M. ;
Castaing, B. ;
Chilla, F. .
PHYSICS OF FLUIDS, 2011, 23 (01)
[38]   Roughness as a Route to the Ultimate Regime of Thermal Convection [J].
Toppaladoddi, Srikanth ;
Succi, Sauro ;
Wettlaufer, John S. .
PHYSICAL REVIEW LETTERS, 2017, 118 (07)
[39]   Tailoring boundary geometry to optimize heat transport in turbulent convection [J].
Toppaladoddi, Srikanth ;
Succi, Sauro ;
Wettlaufer, John S. .
EPL, 2015, 111 (04)
[40]   Effect of surface roughness on heat transfer in Rayleigh-Benard convection [J].
Tummers, Mark J. ;
Steunebrink, Martin .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2019, 139 :1056-1064