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Experimental investigation of mixed convection heat transfer for thermally developing flow in a horizontal circular cylinder

机译:混合对流换热对卧式圆柱热流流动的实验研究

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摘要

An experimental investigation is presented on mixed (free and forced) convection to study the local and average heat transfer for hydrodynamically fully developed, thermally developing and thermally fully developed laminar air flow in a horizontal circular cylinder. The experimental setup consists of aluminum cylinder as test section with 30 mm inside diameter and 900 mm heated length (L/D = 30), is subjected to a constant wall heat flux boundary condition. The investigation covers Reynolds number range from 400 to 1600, the heat flux varied from 60 W/m{sup}2 to 400 W/m{sup}2 and with cylinder inclination angle of θ = 0° (horizontal). The hydrodynamically fully developed condition is achieved by using an aluminum entrance section pipes (calming sections) having the same inside diameter as test section pipe but with variable lengths. The entrance sections included two long calming sections, one with length of 180 cm (L/D = 60), another one with length of 240 cm (L/D = 80) and two short calming sections with lengths 60 cm (L/D = 20), 120 cm (L/D = 40). The surface temperature variation along the cylinder surface, the local and average Nusselt number variation with the dimensionless axial distance Z{sup}+ were presented. For all entrance sections, it was found an increase in the Nusselt number values as the heat flux increases. It was concluded that the free convection effects tended to decrease the heat transfer results at low Re while to increase the heat transfer results for high Re The combined convection regime could be bounded by a suitable selection of Re number ranges and the heat flux ranges. The obtained Richardson numbers (Ri) range varied approximately from 0.13 to 7.125. The average Nusselt numbers were correlated with the (Rayleigh numbers/Reynolds numbers) The proposed correlation has been compared with available literature and showed satisfactory agreement.
机译:对混合(自由和强制)对流进行了实验研究,以研究水平圆柱体内流体动力学充分发展,热发展和热充分发展的层流的局部和平均传热。实验装置由铝制圆柱体作为测试部分组成,该圆柱体的内径为30 mm,加热长度为900 mm(L / D = 30),并经受恒定的壁热通量边界条件。研究覆盖了雷诺数范围从400到1600,热通量从60 W / m {sup} 2到400 W / m {sup} 2的变化,并且圆柱倾斜角为θ= 0°(水平)。通过使用内径与测试段管相同但长度可变的铝制进口段管(压延段),可以达到水力充分发展的条件。入口部分包括两个长的平静区域,一个长度为180厘米(L / D = 60),另一个为长度为240厘米(L / D = 80)和两个较短的平静区域,长度为60 cm(L / D) = 20),120厘米(L / D = 40)。给出了沿汽缸表面的表面温度变化,局部和平均努塞尔数随无因次轴向距离Z {sup} +的变化。对于所有入口部分,发现随着热通量的增加,努塞尔数值也增加。结论是,自由对流效应倾向于降低低Re的传热结果,而增加高Re的传热结果。适当选择Re数范围和热通量范围可以限制组合的对流方式。获得的理查森数(Ri)范围大约在0.13至7.125之间。 Nusselt平均数与(瑞利数/雷诺数)相关。拟议的相关已与现有文献进行了比较,并显示出令人满意的一致性。

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