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Effects of tangential and radial velocity on fluid flow and heat transfer for flow through a pipe with twisted tape insert—laminar flow

机译:切线和径向速度对通过带状扭曲插入件的管道(层流)中流体流动和传热的影响

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The present study reports the numerical analysis of fluid flow and heat transfer in a pipe with full length twisted tape insert. The investigation is carried out for five different twist ratios of 4, 5, 6, 8 and 10 at 100 ≤ Re ≤ 1000. The velocity field in terms of streamwise, tangential and radial velocity and temperature field are studied as a function of Reynolds number and twist ratio. The variation of friction factor and Nusselt number with Reynolds number for different twist ratios is also presented. The heat transfer enhancement due to insertion of twisted tape mainly comes from the tangential and radial components of velocities, which are regarded as secondary fluid motion. It is evident from the results that with increase in Reynolds number the axial convection increases. However, with the decrease in the twist ratio, the tangential and radial convection increases, leading toincreased heat transfer. The secondary flow affects the thermal boundary layer inside the tube and increases the cross-flow mixing, which increases the heat transfer. The correlations for prediction of friction factor and Nusselt number based on the numerical data are also proposed.
机译:本研究报告了带有全长扭曲带插入物的管道中流体流动和传热的数值分析。对100≤Re≤1000的5种不同的扭曲比4,4、5、6、8和10进行了研究。研究了沿流向,切向和径向速度的速度场以及温度场与雷诺数的关系和扭曲比。还给出了不同扭转比下摩擦系数和努塞尔数随雷诺数的变化。由于插入扭曲带而引起的传热增强主要来自速度的切向和径向分量,这些分量被视为二次流体运动。从结果可以明显看出,随着雷诺数的增加,轴向对流增加。但是,随着扭曲比的减小,切向和径向对流增加,从而导致传热增加。二次流影响管内的热边界层并增加错流混合,从而增加热传递。还提出了基于数值数据的摩擦系数和努塞尔数预测的相关性。

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