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Flow felid and heat transfer enhancement investigations by using a combination of corrugated tubes with a twisted tape within 3D circular tube based on different dimple configurations

机译:流动性FELID和传热增强研究通过使用与3D圆形管内的双绞带内的波纹管组合基于不同的凹坑配置

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摘要

Different dimple geometrical configurations with a combination of corrugated tubes and twisted tape are numerically investigated. Water is used as a working fluid for constant heat flux heat transfer conditions at the pipe wall. The dimensionless diameter of the dimples (d/D) used in this study is 0.09, 0.18, 0.27, and 0.36. However, the corrugation configuration diameter is 1 mm. The numerical simulations are carried out at the Reynolds number in the range of 1500-14,000. The outcomes reveal that the friction factor (f) and Nu number are augmented as the dimple diameter increases. The Nu number ratio of 1.25 is found for a dimple pipe tube with a diameter of 4 mm. The numerical outcome presented more mixing, secondary, and vortex produced in the main flow direction and near the pipe wall to the rotating flow induced by twisted tape. Moreover, mixed, secondary vortices and rotational flow originate behind and near the dimple, twisted tape, and corrugation surfaces. These rotational and vortices can promote mixing in flow between the thermal boundary layer and velocity boundary flow layer. So, increase the heat transfer enhancement. The improved pipes with different dimple diameters produce a maximum performance evaluation factor of is more than 1.25.
机译:数值研究了具有波纹管和扭曲胶带的组合的不同凹坑几何配置。水用作管壁处的恒定热通量传热条件的工作流体。本研究中使用的凹坑(D / D)的无量纲直径为0.09,0.18,0.27和0.36。然而,波纹配置直径为1mm。数值模拟在1500-14,000的雷诺数进行。结果表明,随着浊度直径的增加,摩擦因子(F)和NU数被增强。对于直径为4mm的凹坑管,找到了1.25的Nu数比。数值结果呈现在主流量方向和管壁附近产生的更多混合,次级和涡流,以通过扭曲胶带引起的旋转流动。此外,混合,次级涡流和旋转流动源于凹坑,双绞带和波纹表面的后面和附近。这些旋转和涡旋可以促进在热边界层和速度边界流层之间的流动中混合。因此,增加传热增强。具有不同浊度直径的改进管道产生的最大性能评估因子超过1.25。

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