Thermal characteristics in square channel with 45° staggered baffle inserts

S. Kwankaomeng, S. Skullong, T. Teschareon, P. Promvonge
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引用次数: 2

Abstract

The paper presents a study of heat transfer in a heat exchanger channel inserted with staggered inclined baffles. The channel has a square section with uniform wall heat flux conditions. The fluid flow and heat transfer characteristics are presented for Reynolds numbers based on the hydraulic diameter of the channel ranging from 4000 to 25,000. The inclined baffles with an axial pitch equal to three times of channel height and with the attack angle of 45° are mounted in tandem and staggered arrangement on the lower and upper walls of the test channel. Effects of four baffle-to-channel height ratios (e/H = 0.1, 0.2, 0.3 and 0.4) on heat transfer in terms of Nusselt number and pressure loss in the form of friction factor are experimentally investigated. The experimental result shows that the insertion of staggered inclined baffles with the e/H=0.4 provides higher heat transfer and friction factor values than others. This is caused by higher baffle-to-channel height ratios of using e/H = 0.4 interrupting the flow and diverting its direction thus promoting high levels of mixing over others.
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45°交错挡板插入方形通道的热特性
本文研究了插入交错倾斜挡板的换热器通道内的换热问题。该通道为方形截面,壁面热流密度均匀。在4000 ~ 25000雷诺数范围内,给出了流体的流动和换热特性。将轴向节距等于三倍通道高度、攻角为45°的倾斜挡板串联错开安装在试验通道的上下壁上。实验研究了4种挡板与通道高度比(e/H = 0.1、0.2、0.3和0.4)对以努塞尔数表示的换热和以摩擦系数表示的压力损失的影响。实验结果表明,当e/H=0.4时,交错倾斜折流板的传热系数和摩擦系数高于其他折流板。这是由于使用e/H = 0.4的较高挡板与通道高度比中断流动并改变其方向从而促进高水平的混合而造成的。
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