带单侧内肋的矩形水道中已形成湍流和传热的数值研究

IF 0.9 Q4 ENERGY & FUELS Thermal Engineering Pub Date : 2024-03-14 DOI:10.1134/s0040601524020083
V. V. Ris, S. A. Galaev, A. M. Levchenya, I. B. Pisarevskii
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引用次数: 0

摘要

摘要 以燃气轮机叶片内部对流冷却系统的流道为原型,在雷诺数为 5 × 104 到 2 × 105 的范围内,对单侧棱形通道的空间周期模型进行了全展开湍流和展开传热的数值求解。在普朗特数为 0.7 时对流动和传热进行了研究。通道的横截面为矩形,长宽比为 1.5。在其中一个宽通道壁上安装了与通道纵轴成 45° 角的方形肋条,肋条与通道的高度比为 10%。为了量化肋条对流动和传热的影响,将网格合并求解得出的积分参数,如水力阻力系数和努塞尔特数,与相同数值方法预测的光滑渠道中充分发展的流动和传热的积分参数进行了比较。此外,还将带肋水道的数值模拟结果与在部分类似条件下获得的公开实验数据进行了比较。预测的水力阻力系数与实验结果非常吻合。预测的传热量与实验的吻合度在 11% 以内,但数值模拟和物理模拟得出的传热量随雷诺数增加的趋势不同。造成这种差异的原因可能是在短实验通道中无法实现充分发展的传热。通过分析雷诺数与水力阻力系数和努塞尔特数之间的幂律关系,得到了与所有通道壁相关的水力阻力系数和努塞尔特数,而仅与肋壁相关。结果表明,水力阻力系数对雷诺数的依赖性很弱,这是局部阻力的典型表现,而根据问题的具体情况修正后的努塞尔特数的依赖性接近于近壁层和光滑水道中流动的依赖性。
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Numerical Investigation of a Developed Turbulent Flow and Heat Transfer in a Rectangular Channel with Single-Sided Internal Ribs

Abstract

The problem of a fully developed turbulent flow and developed heat transfer was solved numerically at a Reynolds number ranging from 5 × 104 to 2 × 105 for a spatially periodic model of a one-sided ribbed channel as a prototype of the flow path of an internal convective cooling system for a gas turbine blade. The flow and heat transfer were investigated at the Prandtl number of 0.7. The channel has a rectangular cross-section with an aspect ratio of 1.5. Square ribs with a 10% rib-to-channel height ratio are installed on one of the wide channel walls at an angle of 45° to the longitudinal axis of the channel. To quantify the effect of ribs on the flow and heat transfer, the integral parameters, such as hydraulic resistance factor and Nusselt number determined from the grid-converged solutions, are compared with the integral parameters for a fully developed flow and heat transfer in a smooth channel predicted by the same numerical method. The results of numerical simulation for the ribbed channel are also compared with published experimental data obtained under partly similar conditions. The predicted hydraulic resistance factor agrees well with the experiment. The predicted heat transfer agrees with the experiment within 11%, but the trends in heat transfer with increasing Reynolds number obtained using numerical and physical simulation are different. This difference may be caused by the fact that fully developed heat transfer could not be attained in the short experimental channel. Analytical power-law dependences on the Reynolds number are obtained for the hydraulic resistance factor and the Nusselt number pertaining to all channel walls and only to the ribbed wall. It is pointed out that the hydraulic resistance factor depends weakly on the Reynolds number, which is typical for local resistances, and the dependences for Nusselt numbers corrected for the specifics of the problem are close to the dependences for near-wall layers and flows in smooth channels.

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CiteScore
1.30
自引率
20.00%
发文量
94
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