薄膜冷却进口导叶的传热

Marie-Louise Holmer, L. Eriksson, B. Sundén
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引用次数: 5

摘要

采用CFD方法对气膜冷却进口导叶周围的定常流动场和温度场进行了数值模拟。特别计算了外表面温度和传热系数的分布。静压分布也给出了。通过10排气膜冷却孔实现气膜冷却。计算结果与实验数据进行了比较。控制方程由三维有限体积Navier-Stokes求解器求解。采用Wilcox的k-ω湍流模型的低雷诺数版本,以实现湍流情况的计算。应用可实现性约束来减少非物理湍流动能的产生,特别是在前缘附近。为了处理薄膜冷却过程,使用了一个特殊的程序。在计算机代码中实现了一个注入模型。该注入模型在质量、动量、能量和湍流动能方程中,将通过气膜冷却孔的质量流量作为源项加入主流。计算中使用的网格为块结构,网格点总数约为25万个。在一个相关的研究相同的叶片几何,但考虑纯对流传热,作者已经研究了壁面热边界条件的重要性。在此基础上,本文采用了一种共轭传热方法。共轭传热条件是指规定了叶片内表面的传热系数分布,并规定了叶片材料的壁厚和导热系数。然后找到叶片外表面温度作为数值解的一部分。改变了注射模型中的一些基本参数,并发现叶片外表面温度的计算结果与测量结果比较有利。叶片表面静压分布与实验结果吻合较好。马赫数分布提供了流场的信息。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Heat Transfer on a Film Cooled Inlet Guide Vane
The steady flow and temperature fields around a film cooled inlet guide vane are determined numerically by a CFD method. In particular the outer surface temperatures and heat transfer coefficient distributions are calculated. Static pressure distributions are also presented. The film cooling is achieved by 10 rows of film cooling holes. The computed results are compared with experimental data. The governing equations are solved by a 3D finite-volume Navier-Stokes solver. The low Reynolds number version of the k-ω turbulence model by Wilcox is implemented to enable calculations of turbulent flow cases. A realizability constraint is applied to reduce the generation of unphysical turbulent kinetic energy, particularly close to the leading edge. To handle the film cooling process a special procedure is used. An injection model was implemented in the computer code. This injection model adds the mass flow rate passing through the film cooling holes to the main flow as source terms in the equations for mass, momentum, energy and turbulent kinetic energy. The grid used in the calculations is block-structured, and the total number of grid points is around 250,000. In a related investigation for the same vane geometry but considering pure convective heat transfer, the authors have investigated the importance of the wall thermal boundary condition. Based on this a conjugate heat transfer approach was applied in this paper. The conjugate heat transfer condition means that the heat transfer coefficient distribution is prescribed on the inner surface of the vane and also the wall thickness and thermal conductivity of the vane material are prescribed. The vane outer surface temperature is then found as part of the numerical solution. Some essential parameters in the injection model were varied and the calculated results for the vane outer surface temperature were found to compare favourably with measurements. The static pressure distribution on the vane surface agrees well with experiments. The Mach number distribution provides information of the flow field.
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