Studying the Vortex Heat Transfer Enhancement during Turbulent Air Flow over a Plate with a Limited Package of Inclined Oval-Trench Dimples Using Numerical Modeling and Gradient Heatmetry

IF 1.3 Q4 ENERGY & FUELS
S. A. Isaev, S. Z. Sapozhnikov, V. V. Seroshtanov, V. Yu. Mityakov, D. V. Nikushchenko, S. A. Knyazev, A. A. Klyus
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Abstract

The article presents a numerical and experimental study of separated flow and heat transfer in limited packages of four inclined oval-trench dimples (OTDs) located on a heated isothermal section of an adiabatic plate in uniform air flow with the Reynolds number Re = 3 × 104. The depth of dimples is equal to 0.25 of their width, and the angle of inclination is 45°. The isothermal section temperature is maintained with saturated steam. The results of numerical calculations carried out by solving the Reynolds averaged Navier–Stokes equations in the VP2/3 software package, which are closed by the differential equations of the shear stress transfer model (RANS with the SST turbulence model) and the equation of energy, were validated by comparing them with the experimental data obtained by means of gradient heatmetry techniques on the thermophysical setup at the St. Petersburg Polytechnic University. Multiblock computation technologies with the use of intersecting meshes of different scales were applied. It has been found that, with shifting the dimples away from the plate leading edge, relative heat transfer coefficient and back flows are enhanced. With a shift from the first to the fourth dimple, the relative Nusselt number increases in the inlet parts at the bottom by a factor of two (from 1.2 to 2.4) and by a factor of 1.7 (from 1.5 to 2.6) in the windward edge area. The stabilization of stagnation pressure on the windward slopes at a level of 0.26 with the minimal pressure equal to −0.15 in the vortex generation zones entails enhancement of back flows. The static pressure differences cause enhancement of back flows in packaged dimples. The study results have revealed fundamental differences in the heat transfer distribution between the first and subsequent dimples, as well as in their end parts.

Abstract Image

用数值模拟和梯度热法研究带有倾斜椭圆形凹窝的平板上湍流气流的涡流换热增强
本文对雷诺数Re = 3 × 104的均匀气流中位于绝热板受热等温截面上的四个倾斜椭圆沟槽(OTDs)有限封装内的分离流动和换热进行了数值和实验研究。酒窝的深度等于其宽度的0.25,倾斜角为45°。等温段温度由饱和蒸汽维持。通过求解VP2/3软件包中的Reynolds平均Navier-Stokes方程和能量方程的数值计算结果,并将其与圣彼得堡理工大学热物理装置上梯度测热技术获得的实验数据进行了比较,验证了数值计算结果。采用不同尺度相交网格的多块计算技术。研究发现,将凹槽移离板前缘,可以提高相对换热系数和回流。随着从第一个凹窝到第四个凹窝的移动,底部进口部分的相对努塞尔数增加了2倍(从1.2到2.4),迎风边缘区域的相对努塞尔数增加了1.7倍(从1.5到2.6)。迎风坡上的滞止压力稳定在0.26水平,涡产生区最小压力为- 0.15,导致回流增强。静压差导致包装凹窝内回流增强。研究结果揭示了第一个和随后的凹窝之间的传热分布的根本差异,以及在它们的末端部分。
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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来源期刊
CiteScore
1.30
自引率
20.00%
发文量
94
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