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Numerical investigation of the heat transfer and pressure drop on tube bundle support plates for inline and staggered arrangements

机译:直列和交错布置的管束支撑板上传热和压降的数值研究

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Heat transfer and pressure drop characteristics are investigated numerically on tube bundle support plates for inline and staggered arrangements. Three-dimensional numerical analyses within the framework of unsteady Reynolds averaged numerical simulations are performed using four different turbulence models, namely the realisable k-ε, k-ω, SST and transition SST models. In order to reduce the computational effort, simplifications with respect to the domain definition are applied, which were validated within the framework of preliminary studies for assuring accuracy. A constant inlet temperature and a uniform heat flux on the support plates are applied as thermal boundary conditions. The Reynolds number is varied from 989 to 5,550, while keeping the Prandtl number constant at 0.70. The Nusselt number and the pressure drop values are obtained as functions of the Reynolds numbers. The effects of tube bundle arrangements on heat transfer and pressure drop are discussed. Results obtained using different turbulence models are compared with each other and with experiments. The best agreement with the experiments is obtained by the SST model. The least accurate results are provided by the k-ε model. The remaining two turbulence models showed an acceptable performance, close to that of the SST model.
机译:在直列和交错排列的管束支撑板上,数值研究了传热和压降特性。使用四个不同的湍流模型,即可实现的k-ε,k-ω,SST和过渡SST模型,在非稳态雷诺平均数值模拟框架内进行了三维数值分析。为了减少计算量,对域定义进行了简化,并在初步研究的框架内进行了验证,以确保准确性。恒定的入口温度和在支撑板上均匀的热通量被用作热边界条件。雷诺数在989到5,550之间变化,而Prandtl数保持恒定在0.70。根据雷诺数获得努塞尔数和压降值。讨论了管束布置对传热和压降的影响。将使用不同湍流模型获得的结果相互比较并与实验进行比较。通过SST模型可以获得与实验的最佳一致性。 k-ε模型提供的结果最不准确。其余两个湍流模型显示出可接受的性能,接近SST模型。

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