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首页> 外文期刊>Thermal science >THREE-DIMENSIONAL NUMERICAL INVESTIGATION OF TURBULENT FLOW AND HEAT TRANSFER INSIDE A HORIZONTAL SEMI-CIRCULAR CROSS-SECTIONED DUCT
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THREE-DIMENSIONAL NUMERICAL INVESTIGATION OF TURBULENT FLOW AND HEAT TRANSFER INSIDE A HORIZONTAL SEMI-CIRCULAR CROSS-SECTIONED DUCT

机译:水平半圆形横截面管道内湍流和传热的三维数值研究

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摘要

In this study, steady-state turbulent forced flow and heat transfer in a horizontal smooth semi-circular cross-sectioned duct was numerically investigated. The study was carried out in the turbulent flow condition where Reynolds numbers range from 1×104 to 5.5×104. Flow is hydrodynamically and thermally developing (simultaneously developing flow) under uniform surface heat flux with uniform peripheral wall heat flux (H2) boundary condition on the duct’s wall. A commercial CFD program, Ansys Fluent 12.1, with different turbulent models was used to carry out the numerical study. Different suitable turbulence models for fully turbulent flow (k-ε Standard, k-ε Realizable, k-ε RNG, k-ω Standard and k-ω SST) were used in this study. The results have shown that as the Reynolds number increases Nusselt number increases but Darcy friction factor decreases. Based on the present numerical solutions, new engineering correlations were presented for the average Nusselt number and average Darcy friction factor. The numerical results for different turbulence models were compared with each other and similar experimental investigations carried out in the literature. It is obtained that, k-ε Standard, k-ε Realizable and k-ε RNG turbulence models are the most suitable turbulence models for this investigation. Isovel contours of velocity magnitude and temperature distribution for different Reynolds numbers, turbulence models and axial stations in the duct were presented graphically. Also, local heat transfer coefficient and local Darcy friction factor as function of dimensionless position along the duct were obtained in this investigation.
机译:在这项研究中,数值研究了水平光滑半圆形截面管道中的稳态湍流强迫流动和传热。研究是在雷诺数范围从1×104到5.5×104的湍流条件下进行的。在均匀的表面热通量和管道壁上均匀的周壁热通量(H2)边界条件下,流动是流体动力和热发展(同时发展的流动)。使用具有不同湍流模型的商业CFD程序Ansys Fluent 12.1进行了数值研究。在本研究中,使用了不同的适用于全湍流的湍流模型(k-ε标准,k-ε可实现,k-εRNG,k-ω标准和k-ωSST)。结果表明,随着雷诺数的增加,努塞尔数增加,而达西摩擦系数减小。基于当前的数值解,提出了平均努塞尔数和平均达西摩擦因数的新工程相关性。将不同湍流模型的数值结果相互比较,并在文献中进行了类似的实验研究。结果表明,k-ε标准,k-ε可实现和k-εRNG湍流模型是最适合此研究的湍流模型。用图形表示了不同雷诺数,管道中的湍流模型和轴向工位的等速线速度分布和温度分布等值线。而且,在该研究中获得了沿管道的无量纲位置的局部传热系数和局部达西摩擦系数。

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