变管道形状翅片式换热器自然换热实验研究

Mohammed K. Abbas, Hasan K. Abdullah
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摘要

这项工作是一项自然传热的实验研究,从固定在可变形状的风管中加热的圆柱体,由耐热玻璃制成。两个由低碳钢制成的翅片圆柱体,外径(12)mm,内径(10)mm,矩形翅片尺寸(70*40)mm。将两壁与风道的夹角改为5个角α:(0°,3°,5°,10°,15°)与垂直方向形成会聚形状。钢瓶被固定在管道的顶部、中心和底部。采用恒热流密度(88,177,390和680)W/m2)的可变电源加热气缸。研究采用瑞利数(15x103至14x104)。热量由大气空气自由对流携带。实验结果发现,在顶部位置,当角度从0°增加到5°时,努塞尔数在n = 88 W/ m2处增加7.8%;当角度从0°增加到15°时,努塞尔数在n = 680 W/ m2处增加20%。对于中心位置,当角度从0°增加到3°时,努塞尔数在n = 88 W/ m2处增加了25%,当角度从0°增加到10°时,努塞尔数在n = 680 W/ m2处增加了21%。对于底部位置,当角度从0°增加到3°时,nu selt数在n = 88 W/ m2处增加35%;当角度从0°增加到10°时,nu selt数在n = 680 W/ m2处增加30%。换热器的最佳位置为底部,最佳角度为15°。
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Experimental study of natural heat transfer from finned heat exchanger fixed in variable shape of duct
The work was an experimental study of natural heat transfer from heated cylinders fixed in variable shape air duct, made from Pyrex glass. Two finned cylinders made from mild iron, outer diameter (12) mm, inner diameter (10) mm, rectangle fins dimensions (70*40) mm. The angle of two walls from the duct was changed to five angles α:(0°,3°,5°,10°,15°) with vertical to make converge shape. The cylinders were fixed inside the duct at top, centre and bottom. The cylinders were heated by supply variable power of constant heat flux (88,177,390 and 680) W/m2. The study was done with Rayleigh numbers (15x103 to 14x104). The heat was carried by free convection by atmosphere air. The results of experimental found for top location, the value of Nusselt number increased by 7.8% at ԛ•= 88 W/ m2 when increase the value of angle from 0° to 5°, and increased by 20% at ԛ•= 680 W/ m2 when increased the value of angle from 0° to 15°.For centre location, the value of Nusselt number increased by 25 % at ԛ•= 88 W/ m2 when increase the value of angle from 0° to 3°, and increase by 21 % at ԛ•= 680 W/ m2 when increase the value of angle from 0° to 10°.For bottom location, the value of Nusselt number increased by 35 % at ԛ•= 88 W/ m2 when increase the value of angle from 0° to 3°,and increased by 30 % at ԛ•= 680 W/ m2 when increasing the value of angle from 0° to 10°.The best location for the heat exchanger was at the bottom, and the best angle was 15°.
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