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Flow And Heat/mass Transfer In A Wavy Duct With Various Corrugation Angles In Two Dimensional Flow Regimes

机译:在二维流态下具有不同波纹角的波浪形管道中的流动和热/质量传递

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摘要

In this study, two dimensional heat/mass transfer characteristics and flow features were investigated in a rectangular wavy duct with various corrugation angles. The test duct had a width of 7.3 mm and a large aspect ratio of 7.3 to simulate two dimensional characteristics. The corrugation angles used were 100°, 115°, 130°, and 145°. Numerical analysis using the commercial code FLUENT, was used to analyze the flow features. In addition, the oil-lamp black method was used for flow visualization. Local heat/mass transfer coefficients on the corrugated walls were measured using a naphthalene sublimation technique. The Reynolds number, based on the duct hydraulic diameter, was varied from 700 to 5,000. The experimental results and numerical analysis showed interesting and detailed features in the wavy duct. Main flow impinged on upstream of a pressure wall, and the flow greatly enhanced heat/mass transfer. On a suction wall, however, flow separation and reattachment dominantly affected the heat/mass transfer characteristics on the wall. As the corrugation angle decreased (it means the duct has more sharp turn), the region of flow stagnation at the front part of the pressure wall became wider. Also, the position of flow reattachment on the suction wall moved upstream as the corrugation angle decreased. A high heat transfer rate appeared at the front part of the pressure wall due to main-flow impingement, and at the front part of the suction wall due to flow reattachment. The high heat/mass transfer region by the main-flow impingement and the circulation flow induced at a valley between the pressure and suction walls changed with the corrugation angle and the Reynolds number. As the corrugation angle decreased, the flow in the wavy duct changed to transition to turbulent flow earlier.
机译:在这项研究中,研究了具有不同波纹角的矩形波浪形管道中的二维热/质传递特征和流动特征。测试导管的宽度为7.3 mm,宽高比为7.3,以模拟二维特性。所使用的波纹角为100°,115°,130°和145°。使用商业代码FLUENT进行数值分析,以分析流动特征。另外,油灯黑法用于流动可视化。使用萘升华技术测量波纹壁上的局部传热/传质系数。根据管道的液压直径,雷诺数从700到5,000不等。实验结果和数值分析显示出波浪形风管中有趣且详细的特征。主流撞击在​​压力壁的上游,并且该流大大增强了热/质量传递。然而,在吸壁上,流的分离和重新附着主要影响壁上的热/质量传递特性。随着波纹角的减小(这意味着管道具有更大的急转角),压力壁前部的滞流区域变得更宽。而且,随着波纹角的减小,吸壁上的流重新连接的位置向上游移动。由于主流的冲击,在压力壁的前部出现了很高的传热率,而由于流动的重新附着,在吸壁的前部出现了很高的传热率。由主流冲击引起的高热量/质量传递区域以及在压力壁和吸力壁之间的谷处引起的循环流随波纹角和雷诺数而变化。随着波纹角的减小,波浪形管道中的流动更早地转变为湍流。

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