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Numerical simulation of convective heat transfer coefficient in channel with corrugated walls

机译:波纹壁通道对流换热系数的数值模拟

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The present work is a contribution to study of convective heat transfer coefficient inside a rectangular channel with corrugated walls. Triangular, square, and rectangular shaped configurations were studied for a range of geometric parameters during simulation. The Navier-Stokes equations were numerically solved using the finite volume method through the EasyCFD_G package code in its V.4.1.0 version. With prescribed temperatures and velocities, the model predicts the behavior of the air-flow inside the device. The temperature and velocity distributions are first predicted. From these distributions, the convective heat transfer coefficients along the surface of the objects placed inside the system are deter-mined. Also, from the pressure distribution, the pressure drops along the channel are predicted. The results show that the triangular corrugated-shaped configuration with h = 5 cm and α = β = 60° enable to obtain the best value of convective heat transfer coefficient on the surface of the objects which is 2.70 W/m2°C resulting in a pressure drop of 0.11 Pa, while for parallel-plate channel configuration this same coefficient is 1.12 W/m2°C. The energy balance enabled to conclude that the energy gain by convection air/objects is superior to the air pump energy to overcome the pressure drop.
机译:目前的工作为研究波纹壁矩形通道内的对流换热系数做出了贡献。在仿真过程中研究了三角形,正方形和矩形形状的几何参数范围。通过V.4.1.0版中的EasyCFD_G软件包代码,使用有限体积法对Navier-Stokes方程进行了数值求解。在规定的温度和速度下,该模型可以预测设备内部气流的行为。首先预测温度和速度分布。根据这些分布,确定沿放置在系统内部的对象表面的对流传热系数。同样,根据压力分布,可以预测沿通道的压降。结果表明,h = 5 cm和α=β= 60°的三角形波纹状构型能够在物体表面上获得最佳对流传热系数值,即2.70 W / m2°C,从而产生压降为0.11 Pa,而对于平行板通道配置,该系数为1.12 W / m2°C。能量平衡可以得出结论,对流空气/物体的能量获取优于气泵能量,可以克服压降。

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