A COMPREHENSIVE BEJAN'S HEATLINE APPROACH FOR NATURAL CONVECTION HEAT TRANSFER WITHIN INCLINED SQUARE CAVITIES

被引:0
作者
Singh, Abhishek Kumar [1 ]
Roy, S. [1 ]
Basak, Tanmay
机构
[1] Indian Inst Technol, Dept Math, Madras 600036, Tamil Nadu, India
来源
PROCEEDINGS OF THE ASME SUMMER HEAT TRANSFER CONFERENCE, 2012, VOL 1 | 2012年
关键词
VISUALIZATION; STREAMLINE; MASSLINE;
D O I
暂无
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
The present study deals with natural convection heat transfer within water (Pr = 7.2) filled inclined square cavities for hot bottom wall (case 1: isothermal heating/case 2: non-isothermal heating) and cold side walls in the presence of adiabatic top wall. The Galerkin finite element method has been used to solve the nonlinear coupled partial differential equations governing the fluid flow and thermal fields. This method is further used to solve the Poisson equation for streamfunction and heatfunction. The streamlines (psi), isotherms (theta) and heatlines (Pi) are obtained for various inclination angles (phi = 0 degrees, 30 degrees and 60 degrees) in the range of Rayleigh numbers (10(3) <= Ra <= 10(5)). The physical significance of heatlines have been demonstrated for a comprehensive understanding of heat energy distribution within the inclined square cavities. The flow pattern is symmetric for phi = 0 degrees whereas asymmetric flow pattern is observed for the phi = 30 degrees and 60 degrees due to tangential and normal components of buoyancy forces. At Ra = 10(3), weak fluid circulation and orthogonal heatlines on isothermal surface, indicate conduction dominant heat transfer for both cases. Strong closed loop heatlines are found due to strong fluid convective circulation cells at Ra = 10(5). Heat transfer rates are obtained in terms of local and average Nusselt numbers. In general, the overall amount of heat transfer along the right wall increases with inclination angle and that decreases along the left wall with increase in inclination angle. The non-isothermal heating case exhibits greater heat transfer rates at the center of the bottom wall than the isothermal heating whereas average Nusselt number shows that overall heat transfer rate is larger for the isothermal heating case as compared to that of non-isothermal heating case.
引用
收藏
页码:1067 / 1076
页数:10
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