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Início - ICHMT DL Ano atual Arquivos Comitê executivo Centro Internacional para Transferência de Calor e Massa


Ya-Ling He
Key Laboratory of Thermo-fluid Science and Engineering, Ministry of Education, School of Energy and Power Engineering, Xi'an Jiaotong University, Xi'an, Shaanxi 710049, China

Wei-Wei Yang
School of Energy and Power Engineering, Xi'an Jiaotong University, Xi'an, Shaanxi, 710049 China

Wen-Quan Tao
State Key Laboratory of Pollution Control and Resources Reuse, College of Environmental Science & Engineering, Tongji University, Shanghai 200092, China; Key Laboratory of Thermo-Fluid Science and Engineering of MOE, School of Energy and Power Engineering, Xian Jiaotong University, Xian 710049, China


Steady-state laminar natural convection in a cubic enclosure with a cold vertical wall and two hot square heaters on the opposite wall is studied numerically. The enclosure is filled with various liquids. Three-dimensional form of Navier-Stokes equations are solved by employing SIMPLE algorithm. Computations are performed for a range of Rayleigh number from 103 to 107 while enclosure aspect ratio varies from 0.05 to 1.6. The effects of Rayleigh number, enclosure aspect ratio and Prandtl number on heat transfer characteristics are studied in detail. The results show that the flow field is very complex and heat transfer from the heaters is not uniform. The effects of Prandtl number are negligible in the range from 5 to 140 with other parameters keeping constant. This allows the use of liquids such as water for studying other dielectric liquids provided the flow geometry and other non-dimensional parameters are similar. The overall Nusselt number increases with Rayleigh number markedly. It also is affected by enclosure aspect ratio. It attains the maximum value when aspect ratio is in the range of 0.05−0.3 and decreases as enclosure aspect ratio varies from 0.3 to 1.6. Also various settings of cooling face and arrangement of heaters are studied, the results showing that these have considerable effects on heat transfer of both heaters.

ICHMT Digital Library

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