Numerical Simulation of Turbulent Flow and Heat Transfer in an Anti- Gravity Blind Duct with Tangential Entry Jet

S. Chang, Zong-Xian Cai
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引用次数: 3

Abstract

This numerical study investigates the flow and heat transfer characteristics in a vertical square blind duct with the coolant fed by a tangential entry jet. The detailed Nusselt number (Nu) distributions over the five constituent walls of the blind duct are calculated at duct (jet) Reynolds numbers Re(Rej) of 5000(20000), 7000(28000) and 10000(40000) us- ing the commercial CFD Star CD code. As an attempt to explore the buoyancy effect on heat transfer performances, three different heat fluxes, which vary the gravitational Grashof numbers (Grg) at the fixed Re, are imposed on each duct wall to vary the buoyancy levels. The jet-induced flow phenomena in the blind duct exhibit various heat transfer impacts on the five duct walls over which the different near-wall flow structures are generated. This is demonstrated by cross-examining the detailed Nu distributions and the area-averaged Nusselt number ( Nu ) over the five duct walls at the tested Re and Grg. The cross-plane swirls induced by the tangential entry jet together with the impinging jet flows considerably elevate the Heat Transfer Enhancement (HTE) performances in the blind duct. Within the parametric conditions simulated, the ratios of Nu to the Dittus-Boelter levels (Nu� ) over the jet wall, back wall, impingement wall, side wall and end wall are re- spectively raised to 3-5.7, 2.8-5.6, 3-5.8, 2.7-4.8 and 3.1-6.1; while the HTE ratios ( Nu /Nu� ) over these duct walls con- sistently decrease as Re increases.
具有切向入口射流的反重力盲管湍流流动和传热的数值模拟
本文研究了垂直方形盲管中切向入口射流供冷剂的流动和换热特性。利用商业CFD Star CD代码,在风管(射流)雷诺数Re(Rej)分别为5000(20000)、7000(28000)和10000(40000)时,计算了盲管五个组成壁上的努塞尔数(Nu)的详细分布。为了探索浮力对传热性能的影响,在固定Re处施加三种不同的热流,改变重力格拉什夫数(Grg),以改变每个管道壁上的浮力水平。射流诱导的盲管流动现象在不同的管壁上表现出不同的换热影响,在不同的管壁上产生不同的近壁流动结构。这可以通过交叉检查详细的Nu分布和在测试Re和Grg处五个管道壁上的面积平均努塞尔数(Nu)来证明。切向入口射流与冲击射流形成的交叉平面涡漩显著提高了盲管内的传热强化性能。在模拟的参数条件下,射流壁、后壁、冲击壁、侧壁和端壁上Nu与Dittus-Boelter水平的比值分别提高到3-5.7、2.8-5.6、3-5.8、2.7-4.8和3.1-6.1;而随着Re的增加,这些管道壁上的HTE比率(Nu /Nu′)一致降低。
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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