Applied Mathematics and Mechanics (English Edition) ›› 2021, Vol. 42 ›› Issue (8): 1183-1190.doi: https://doi.org/10.1007/s10483-021-2754-5

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Horizontal convection in a rectangular enclosure driven by a linear temperature profile

Tianyong YANG, Bofu WANG, Jianzhao WU, Zhiming LU, Quan ZHOU   

  1. Shanghai Key Laboratory of Mechanics in Energy Engineering, Shanghai Institute of Applied Mathematics and Mechanics, School of Mechanics and Engineering Science, Shanghai University, Shanghai 200072, China
  • Received:2021-03-29 Revised:2021-06-02 Published:2021-07-28
  • Contact: Jianzhao WU, E-mail:jianzhao wu@shu.edu.cn
  • Supported by:
    the National Natural Science Foundation of China (Nos. 11988102, 92052201, 11972220, 11825204, 91852202, and 11732010), the China Postdoctoral Science Foundation (No. 2020M681259), and the Key Research Projects of Shanghai Science and Technology Commission (Nos. 19JC1412802 and 20ZR1419800)

Abstract: The horizontal convection in a square enclosure driven by a linear temperature profile along the bottom boundary is investigated numerically by using a finite difference method. The Prandtl number is fixed at 4.38, and the Rayleigh number Ra ranges from 107 to 1011. The convective flow is steady at a relatively low Rayleigh number, and no thermal plume is observed, whereas it transits to be unsteady when the Rayleigh number increases beyond the critical value. The scaling law for the Nusselt number Nu changes from Rossby’s scaling Nu~Ra1/5 in a steady regime to NuRa1/4 in an unsteady regime, which agrees well with the theoretically predicted results. Accordingly, the Reynolds number Re scaling varies from Re~Ra3/11 to Re~Ra2/5. The investigation on the mean flows shows that the thermal and kinetic boundary layer thickness and the mean temperature in the bulk zone decrease with the increasing Ra. The intensity of fluctuating velocity increases with the increasing Ra.

Key words: horizontal convection, linear temperature profile, turbulent heat transfer, boundary layer

2010 MSC Number: 

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