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Numerical analysis of flow and heat transfer enhancement in a horizontal pipe with P-TT and V-Cut twisted tape

机译:用P-TT和V-Cut扭曲带增强水平管中流动和传热的数值分析

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In this work, forced convection heat transfer through a horizontal pipe built-in with/without twisted tape-inserts is numerically studied under a uniform heat flux condition. Water is used as a working fluid. The governing equations are numerically solved in the domain by a finite volume method (FVM) using the Realizable κ–ε (RKE) model. The computational results are performed for a range of the Reynolds number (4000?≤?Re?≤?9000), the twisted ratio (4.0?≤?TR?≤?6.0), and heat flux (5000?≤?q?≤?1000?W/m2). Two type of twisted tape which inserts across a circular pipe (P-TT) and (V-cut) are carried out. The influence of these parameters on the local, average Nusselt Number and the thermal performances were examined and compared with a plain pipe under similar conditions. The results show that the average Nusselt number and friction factor raise as the twisted ratio rise for any value of Reynolds number. Furthermore, thermal performance factor tended to increase with increasing Re and decreasing tape twist ratio. Obviously, the (V-cut) twisted- tape and (P-TT) twisted tape with TR?=?4 gave a higher mean thermal performance factor (4.45, and 4.19) than that with TR?=?6, respectively. Finally, the present study can offer some useful results to select optimum geometrical parameters for use in shell and tube heat exchangers with a twisted tape inserted based on their specific applications.
机译:在这项工作中,在均匀的热通量条件下,通过数值研究了通过带/不带扭转带状插入件的水平管道内置的强制对流传热。水被用作工作流体。使用可实现的κ–ε(RKE)模型,通过有限体积法(FVM)在域中对​​控制方程进行数值求解。计算结果是针对雷诺数(4000?≤?Re?≤?9000),扭曲比(4.0?≤?TR?≤?6.0)和热通量(5000?≤?q?≤ ?1000?W / m2)。进行了两种缠绕在圆管上的扭曲胶带(P-TT)和(V形切口)。检查了这些参数对局部平均努塞尔数和热性能的影响,并在类似条件下与普通管进行了比较。结果表明,对于任何雷诺数,平均努塞尔数和摩擦系数都随着扭曲比的增加而增加。此外,热性能因数趋于随Re的增加和胶带扭曲率的降低而增加。显然,TRδ=α4的(V-cut)双绞带和(P-TT)绞合带的平均热性能因数(TR5 =β6)分别更高(4.45和4.19)。最后,本研究可以提供一些有用的结果,以根据其特定应用选择用于插入扭曲带的管壳式热交换器的最佳几何参数。

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