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Experimental study on flow and local heat/mass transfer characteristics inside corrugated duct

机译:波纹管内流动和局部传热/传质特性的实验研究

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The present study investigates the flow and heat/mass transfer characteristics of wavy duct for the primary surface heat exchanger application. Local heat/mass transfer coefficients on the corrugated duct side walls are measured using a naphthalene sublimation technique. The flow visualization technique and a numerical analysis using a commercial code, FLUENT, are used to understand the overall flow structures inside the duct. The corrugation angle of the wavy duct is 145° and the duct aspect ratio is 7.3. The Reynolds numbers, based on the duct hydraulic diameter, vary from 100 to 5000. The results show that complex secondary flows and transfer processes exist inside the wavy duct resulting in non-uniform distributions of the heat/mass transfer coefficients on the duct side walls. At low Reynolds numbers (Re ≤ 1000), relatively high heat/mass transfer regions like cell shapes appear on both pressure- and suction-side walls due to the secondary vortex flows called Taylor-Goertler vortices perpendicular to the main flow direction. However, at high Reynolds numbers (Re > 1000), these secondary flow cells disappear and boundary layer type flow develop on pressure-side wall. On the suction-side wall, high heat/mass transfer region appears by the flow reattach-ment. The average heat/mass transfer coefficients are higher than those of the smooth circular duct and pressure drop increases due to the secondary flows inside wavy duct.
机译:本研究研究了用于初级表面热交换器的波浪形管道的流量和传热/传质特性。使用萘升华技术测量波纹管侧壁上的局部传热/传质系数。流量可视化技术和使用商业代码FLUENT的数值分析用于了解管道内部的总体流量结构。波浪形导管的波纹角为145°,导管的纵横比为7.3。基于管道水力直径的雷诺数在100到5000之间变化。结果表明,波浪形管道内部存在复杂的二次流和传热过程,导致传热/传质系数在管道侧壁上的分布不均匀。 。在低雷诺数(Re≤1000)下,由于称为垂直于主流方向的泰勒-戈特勒涡流的二次涡流,在压力和吸力侧壁上都出现了相对较高的传热/传质区域,如气泡形状。但是,在高雷诺数(Re> 1000)时,这些二次流动池消失,边界层型流动在压力侧壁上发展。在吸力侧壁上,通过流量重新连接出现了高热量/质量传递区域。平均传热/传质系数高于光滑圆形导管,并且由于波浪形导管内的二次流动,压降增加。

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