Experimental Study of Forced Convection Heat Transfer Porous Media inside a Rectangular Duct at Entrance Region

M. Hasan, S. Rasheed, A. N. Mahdi
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引用次数: 2

Abstract

This work presents experimental investigation of flow and heat transfer characteristics for entry length of turbulent flow in a rectangular duct fitted with porous media and air as the working fluid. Rectangular duct (300×30 mm) with a hydraulic diameter (54.54 mm) was subjected to constant heat flux from lower surface (1.5 ×102 –1.8 ×102 w/m2) and Reynolds number ranged (3.3x104 up to 4.8x104). Copper mesh inserts (as porous media) with screen diameter (54.5 mm) for vary distance between two adjacent screens of (10 mm), (15 mm) and (20 mm) in the porosity range of (0.98 - 0.99) are considered for experimentation. The effect of porous height ratio (full and partial) are also considered. It is observed that the enhancement of heat transfer by using mesh inserts when compared to a plain surface is more by a factor of (2.2) times where the skin fraction coefficient is about (5) times. An Empirical correlation for Nusselt number and friction factor are developed for the mesh inserts from the obtained results.
矩形管道入口区多孔介质强制对流换热实验研究
本文通过实验研究了以多孔介质和空气为工质的矩形管道中湍流入口长度的流动和传热特性。水压直径为54.54 mm的矩形风管(300×30 mm)承受恒定的下表面热通量(1.5 ×102 -1.8 ×102 w/m2),雷诺数范围为3.3x104至4.8x104。在孔隙率(0.98 - 0.99)范围内,两个相邻筛网之间的距离为(10mm)、(15mm)和(20mm),筛网直径为(54.5 mm)的铜网插入物(作为多孔介质)被考虑用于实验。同时考虑了孔隙高度比(全部和部分)的影响。可以观察到,与平面表面相比,使用网格插入对传热的增强作用是(2.2)倍,其中皮肤分数系数约为(5)倍。根据所得结果,推导出了啮合件的努塞尔数与摩擦因数的经验相关关系。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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