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3D numerical and experimental analysis for thermal-hydraulic characteristics of air flow inside a circular tube with different tube inserts

机译:具有不同管插入件的圆形管内气流的热工水力特性的3D数值和实验分析

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Numerical and experimental analyses were carried out to study thermal-hydraulic characteristics of air flow inside a circular tube with different tube inserts. Three kinds of tube inserts, including longitudinal strip inserts (both with and without holes) and twisted-tape inserts with three different twisted angles (α = 15.3°, 24.4° and 34.3°) have been investigated for different inlet frontal velocity ranging from 3 to 18 m/s. Numerical simulation was performed by a 3D turbulence analysis of the heat transfer and fluid flow. Conjugate convective heat transfer in the flow field and heat conduction in the tube inserts are considered also. The experiments were conducted in a shell and tube exchanger with overall counterflow arrangement. The working fluid in the tube side was cold air, while the hot Dowtherm fluid was on the shell side. To obtain the heat transfer characteristics of the test section from the experimental data, the ε-NTU (effectiveness-number of transfer unit) method is applied to determine the overall conductance (UA product) in the analysis. It was found that the heat transfer coefficient and the pressure drop in the tubes with the longitudinal strip inserts (without hole) were 7-16% and 100-170% greater than those of plain tubes without inserts. When the longitudinal strip inserts with holes were used, the heat transfer coefficient and the pressure drop were 13-28% and 140-220%, respectively, higher than those of plain tubes. The heat transfer coefficient and the pressure drop of the tubes with twisted-tape inserts were 13-61% and 150-370%, respectively, higher than those of plain tubes. Furthermore, it was found that the reduction ratio in the heat transfer area of the tube of approximately 18-28% may be obtained if the twisted-tape tube inserts are used.
机译:进行了数值和实验分析,以研究具有不同管插入件的圆形管内部的空气流的热工水力特性。研究了三种管件,包括纵向条形插件(带孔和不带孔)和具有三种不同扭曲角度(α= 15.3°,24.4°和34.3°)的扭曲带插件,其入口速度范围为3到3。至18 m / s。通过对传热和流体流动的3D湍流分析进行了数值模拟。还考虑了流场中的共轭对流传热和管插件中的热传导。实验在具有整体逆流布置的壳管式交换器中进行。管侧的工作流体是冷空气,而热的道氏热流体在壳侧。为了从实验数据中获得测试部分的传热特性,应用ε-NTU(传递单位的效率数)方法确定分析中的总电导率(UA乘积)。发现带有纵向条形插入件(无孔)的管子的传热系数和压降比没有插入件的普通管子的传热系数和压降大了7-16%和100-170%。当使用带有孔的纵向条形插入件时,传热系数和压降分别比普通管的传热系数和压降高13-28%和140-220%。带扭带插入件的管子的传热系数和压降分别比普通管子高13-61%和150-370%。此外,发现如果使用扭曲带管插入件,则可以在管的传热区域中获得大约18-28%的减小率。

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