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Numerical analysis of ball-type turbulators in tube heat exchangers with computational fluid dynamic simulations

机译:计算流体动态模拟管式热交换器中球型湍流的数值分析

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In the tube heat exchangers, heat transfer enhancement by creation of turbulent flow has been investigated in a number of previous research using different turbulator forms and methods, whereas in the present work a novel ball-type turbulators is used as a new technique implementation to increase heat transfer rate by vortex generation in the flow. Numerical analysis is performed for proposed novel turbulator to probe heat and flow characteristics. Ball-type turbulators have been designed in three different ball diameters inside a tube exchanger. The effects of balls diameter, pitches and Reynolds number on the heat transfer, friction factors and also entropy generation are analyzed at four different Reynolds numbers between 5000 and 20,000. The Nusselt number and friction factor outcomes are compared with those of smooth tube under the same flow and thermal conditions to determine the heat transfer enhancement. From the numerical analysis, it is specified that the suggested turbulators generate a larger vortex flow at low Reynolds numbers, and consequently, more effective heat transfer can be obtained. Moreover, increasing the ball diameter will lead to more heat transfer rate due to the wider vortex region at behind of the ball.
机译:在管热交换器中,通过不同的湍流形成和方法在许多先前研究中研究了湍流的热传递增强,而在本工作中,新颖的球型湍流器用作增加的新技术实现通过流动中的涡流产生传热速度。对提出的新型湍流器进行数值分析,用于探测热流和流动特性。球型湍流器已经设计成三个不同的球直径在管道交换机内。在传热,摩擦因子和熵产生的球直径,俯仰和雷诺数的影响在5000到20,000之间的四个不同的雷诺数。在相同的流动和热条件下与光滑管相比,尤塞格数和摩擦因子结果进行比较,以确定热传递增强。根据数值分析,指定所建议的湍流器在低雷诺数产生较大的涡流流动,因此,可以获得更有效的传热。此外,由于球后面的较宽的涡流区域,增加球直径将导致更多的传热速率。

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