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摘要

在许多工程应用中,如燃气涡轮发动机,燃烧器,加热和冷却系统,分离和再附着区域是由于向后的阶跃流而产生的。控制这些区域对于增加传热和传质是非常重要的。为了考察流动分离和再附着的影响,在垂直定位后面向台阶流动几何中,数值研究了无倒角(法向)几何中不同倒角长度h/4和h/2阶角结构的传热和流动特性。后台阶后面的一个壁保持恒定温度,而其他壁是绝热的。利用ANSYS-FLUENT计算程序,用Boussinesq法求解三维稳态k-ε湍流模型的守恒方程,得到了研究结果。水和液态钠被用作工质。后向台阶膨胀率为1.5。在5000和10000两种不同的雷诺数下进行了研究。本研究已与文献中发现的工作的数值结果进行了比较,发现它们是相互兼容和可接受的。结果表现为努数、流体温度、湍流动能和压力的变化。此外,温度,速度和流线分布已经可视化的面向后阶流几何。当Re=5000时,确定了液钠流动中无倒角(法向)阶跃几何的平均Nu值比倒角长度为h/2的后向阶跃几何高9%。
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Geriye Dönük Adım Akışında Adım Geometrisinin Isı Transferi ve Akış Yapısı Üzerindeki Etkisinin İncelenmesi
In many engineering applications such as gas turbine engines, burners, heating and cooling systems, separation and reattachment areas occur due to the backward-facing step flow. Control of these areas is very important to increase the amount of heat and mass transfer. In this study, in order to examine the effect of flow separation and reattachment, the heat transfer and flow characteristics of step corner structures with different chamfer lengths as h/4 and h/2 according to without chamfer (normal) geometry have been numerically researched in the vertically positioned backward-facing step flow geometry. One of the walls behind the backward-facing step has been kept at a constant temperature while the others are adiabatic. The results of the study have been obtained by solving conservation equations with three dimensional and steady k-ε turbulence model with Boussinesq approach using ANSYS-FLUENT computer program. Water and liquid sodium have been used as working fluids. Expansion rate of the backward-facing step is 1.5. The work has been performed at different Reynolds numbers as 5000 and 10000. The present study has been compared with the numerical results of the work found in the literature and it has been found that they are compatible and acceptable with each other. The results have been presented as the variations of Nu number, fluid temperature, turbulence kinetic energy and pressure. In addition, temperature, velocity and streamline distributions have been visualized in backward-facing step flow geometry. For Re=5000, the average Nu number value of the step geometry without chamfer (normal) in the liquid sodium flow has been determined to be 9% higher than the backward-facing step geometry with h/2 chamfer length.
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