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首页> 外文期刊>Thermal science >EXPERIMENTAL STUDY OF DEVELOPING TURBULENT FLOW AND HEAT TRANSFER IN RIBBED CONVERGENT/DIVERGENT RECTANGULAR DUCTS
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EXPERIMENTAL STUDY OF DEVELOPING TURBULENT FLOW AND HEAT TRANSFER IN RIBBED CONVERGENT/DIVERGENT RECTANGULAR DUCTS

机译:带肋汇流/扩散矩形导管中湍流和传热发展的实验研究

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摘要

The article represents an experimental investigation of friction and heat transfer characteristics of divergent / convergent rectangular ducts with an inclination angle of 1˚ in the y-axis. Measurements were taken for a convergent / divergent rectangular duct of aspect ratio AR at inlet1.25 and outlet in convergent channel 1.35; but in case of divergent duct it can be reversed. The four uniform rib heights, e = 3, 6, 9 and 12 mm the ratio between rib height to hydraulic mean diameter (e/Dm) are 34.8, 69.7, 104.6 and 138.7 a constant rib pitch distance, P = 60 mm has been used. The flow rate in terms of average Reynolds number based on the hydraulic mean diameter (Dm) is 86 mm of the channel was in a range of 20,000 to 50,000. The two ceramic heating strip of 10 mm thickness is used as a heating element have attached on top and bottom surfaces for the test sections. The heat transfer performance of the divergent / convergent ducts for 3, 6, 9 and 12 mm ribs was conducted under identical mass flow rate based on the Reynolds number. In our experiments has totally 8 different ducts were used. In addition, the acceleration / deceleration caused by the cross section area, the divergent duct generally shows enhanced heat transfer behavior for four different rib sizes, while the convergent duct has an appreciable reduction in heat transfer performance. From result point view divergent duct with 3 mm height ribbed square duct gets maximum heat transfer coefficient with minimum friction loss over the other convergent / divergent ducts.
机译:这篇文章代表了在y轴上倾斜角度为1°的发散/会聚矩形管道的摩擦和传热特性的实验研究。在汇合通道1.35的入口1.25和出口处测量长宽比为AR的会聚/发散矩形风道。但如果导管发散,则可以将其反转。四个均匀的肋高e = 3、6、9和12 mm,肋高与液压平均直径(e / Dm)之比为34.8、69.7、104.6和138.7,肋间距不变,P = 60 mm用过的。基于基于液压平均直径(Dm)的平均雷诺数的流量为86mm,通道的范围为20,000至50,000。厚度为10 mm的两个陶瓷加热条被用作加热元件,并附在测试部分的顶部和底部。基于雷诺数,在相同的质量流量下,对3、6、9和12 mm肋进行扩/缩管的传热性能。在我们的实验中,总共使用了8种不同的风管。另外,由横截面面积引起的加速/减速,发散导管通常对于四种不同的肋尺寸显示出增强的传热性能,而会聚导管的传热性能显着降低。从结果角度看,具有3 mm高度的肋形方管的分叉管与其他会合/分叉管相比,具有最大的传热系数和最小的摩擦损失。

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