Vishwakarma Devendra Kumar, Bhattacharyya Suvanjan, Soni Manoj K
Department of Mechanical Engineering, BITS Pilani, Pilani Campus, Pilani, RJ, 333031, India.
Center of Excellence for Electronics Cooling and Computational Fluid Dynamics Simulation Lab, SRMIST, SRM Nagar, Kattankulathur, Chengalpattu District, TN, 603 203, India.
Sci Rep. 2024 Nov 12;14(1):27640. doi: 10.1038/s41598-024-75337-w.
The research involves an experimental investigation into the performance of a flow assisting air heat exchanger under varying angular orientation and uniform external heat fluxes without and with spring turbulators. The investigation was performed for Reynolds numbers ranging from 511 to 9676 and inclination angle 15° and 30°. Three heat fluxes (2, 3, and 4 kW/m) were applied to the test section to investigate the effect of external surface heating on the range of transition flow regime and thermohydraulic performance. Transition from laminar to turbulent flow for plain channel at different heat fluxes and inclinations occurs within specific Reynolds number ranges: 2436-4446 for 15° inclination at 4 kW/m, 2574-4289 at 3 kW/m, and 2850-4152 at 2 kW/m; for 30° inclination, the ranges are 2518-4151, 2712-4361, and 2992-4346 at the respective heat fluxes. When it comes to the effect of inclination on Nusselt number, the transition occurs sooner at lower angles, but is delayed as the angle increases. Additionally, the Nusselt number decreases as the angle of inclination increases. When comparing the Nusselt numbers of plain tubes to those with spring turbulators, the latter shows a significantly greater enhancement. In laminar flow, a maximum 100% deviation exists between highest and lowest friction factors, decreasing to 75% with increasing Reynolds number; all insert configurations exhibit highest friction factor at 15° due to stronger buoyancy forces.
该研究涉及对一种流动辅助空气热交换器在不同角度取向以及有无弹簧扰流器情况下、在均匀外部热通量作用下的性能进行实验研究。研究针对雷诺数范围为511至9676以及倾斜角为15°和30°的情况展开。向测试段施加了三种热通量(2、3和4kW/m²),以研究外表面加热对过渡流态范围和热工水力性能的影响。对于光滑通道,在不同热通量和倾斜角度下从层流到湍流的转变发生在特定的雷诺数范围内:在4kW/m²时,15°倾斜角下为2436 - 4446;3kW/m²时为2574 - 4289;2kW/m²时为2850 - 4152。对于30°倾斜角,在相应热通量下的范围分别为2518 - 4151、2712 - 4361和2992 - 4346。当涉及倾斜对努塞尔数的影响时,较低角度下转变发生得更早,但随着角度增加而延迟。此外,努塞尔数随着倾斜角的增加而减小。当将光滑管的努塞尔数与带有弹簧扰流器的管的努塞尔数进行比较时,后者显示出显著更大的增强。在层流中,最高和最低摩擦系数之间存在最大100%的偏差,随着雷诺数增加降至75%;由于浮力更强,所有插入配置在15°时都表现出最高的摩擦系数。