首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Experimental and numerical investigation of turbulent nanofluid flow in helically coiled tubes under constant wall heat flux using Eulerian-Lagrangian approach
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Experimental and numerical investigation of turbulent nanofluid flow in helically coiled tubes under constant wall heat flux using Eulerian-Lagrangian approach

机译:欧拉-拉格朗日方法在恒定壁热通量下螺旋盘管内纳米湍流的实验和数值研究

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In the present study, turbulent flow in helically coiled tubes under constant wall heat flux is numerically and experimentally investigated. Pressure drop and convective heat transfer behavior of water and water-silver nanofluid are studied. In experimental section, the pressure drop measurements as well as the average convective heat transfer coefficient calculations are carried out. The numerical computations are performed by Eulerian-Lagrangian two-phase approach in connection with an RNG k-epsilon turbulence model accounting for four-way coupling collisions using ANSYS CFX software. The Brownian motion of nanoparticles is taken into account. Single-phase approach (homogeneous model with constant effective properties) is also used. Two-phase approach predicted much more accurate results than the homogeneous model. More enhanced heat transfer was observed for tubes with greater curvature ratio. The results showed that the nanoparticles did not change the axial velocity and turbulent kinetic energy significantly, while the micrometer-sized particles increased mean axial velocity and suppressed turbulence. It was found that the utilization of the base fluid in helical pipe with greater curvature ratio compared to the use of nanofluid in straight tubes increased heat transfer more effectively. Based on the numerical results validated by the experimental ones, two correlations were developed to predict the ratio of the mean heat transfer coefficient and the pressure drop of nanofluid to water in helical tubes. (C) 2014 Elsevier B.V. All rights reserved.
机译:在本研究中,在恒定壁热通量的情况下,对螺旋盘管中的湍流进行了数值和实验研究。研究了水和水银纳米流体的压降和对流传热行为。在实验部分,进行了压降测量以及平均对流传热系数的计算。数值计算是通过Eulerian-Lagrangian两阶段方法结合RNGk-ε湍流模型进行的,并使用ANSYS CFX软件解决了四向耦合碰撞问题。考虑了纳米粒子的布朗运动。也使用单相方法(具有恒定有效特性的均质模型)。两阶段方法比均匀模型预测的结果准确得多。对于具有较大曲率比的管,观察到更多的热传递。结果表明,纳米颗粒没有明显改变轴向速度和湍动能,而微米级颗粒增加了平均轴向速度并抑制了湍流。已经发现,与在直管中使用纳米流体相比,在曲率比更大的螺旋管中利用基础流体更有效地增加了热传递。根据实验验证的数值结果,建立了两种相关性,以预测螺旋管中纳米流体对水的平均传热系数与压降之比。 (C)2014 Elsevier B.V.保留所有权利。

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