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Experimental and numerical investigation of heat and fluid flow in a square duct featuring criss-cross rib patterns

机译:方形管道中的热量和流体流动的实验性和数值研究

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摘要

This paper presents findings from experimental and numerical study of heat and fluid flow in a straight square duct featuring rib turbulators in a criss-cross pattern formed by 450 angled rib turbulators. Two ribbed configurations with criss-cross pattern - Inline and staggered, have been studied where the baseline case was smooth duct with no heat transfer enhancement feature. Detailed heat transfer coefficients were calculated using transient liquid crystal thermography by employing 1-D semi-infinite conduction model. Heat transfer and pressure drop measurements were carried out for Reynolds number ranging from 30,000 to 60,000. For understanding of heat transfer enhancement mechanism, numerical investigations were carried out using SST k-omega turbulence model. Numerical predictions of near-wall fluid dynamics and turbulent transport has been presented in conjunction with experimentally obtained detailed heat transfer coefficients to demonstrate the heat transfer characteristics of ribbed duct. Nusselt numbers normalized with respect to Dittus-Boelter correlation for developed turbulent flow in circular duct varied between 2.7 and 3.1 for inline and staggered configurations and the thermal hydraulic performance varied between 1.2 and 1.5 for the range of Reynolds number investigated. (C) 2017 Elsevier Ltd. All rights reserved.
机译:本文介绍了一种直方体管道中的热量和流体流动的实验性和数值研究的结果,其具有由450角度肋湍流器形成的十字交叉图案的肋湍流器。已经研究了两大罗纹配置,载有纵横交错模式 - 内联和交错,其中基线外壳是光滑的管道,没有传热增强功能。通过采用1-D半无限传导模型,使用瞬态液晶热成像计算详细的传热系数。为雷诺数的传热和压降测量范围为30,000至60,000。为了理解热传递增强机制,使用SST k-Omega湍流模型进行数值研究。已经结合实验获得的详细传热系数来呈现近壁流体动力学和湍流传输的数值预测,以证明肋状管道的传热特性。对于在圆形管道中发育湍流的DTTUS-FABENT流量的纽扣数量归一化的纽带数在2.7和3.1之间变化,内联和交错的配置,并且在研究的雷诺数范围内的热液压性能之间变化为1.2和1.5。 (c)2017 Elsevier Ltd.保留所有权利。

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