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多壁碳纳米管/水纳米流体双螺旋盘管换热器热与流动特性的计算流体动力学分析

CFD analysis on heat and flow characteristics of double helically coiled tube heat exchanger handling MWCNT/water nanofluids.

作者信息

Mukesh Kumar P C, Chandrasekar M

机构信息

Department of Mechanical Engineering, University College of Engineering, Dindigul, Tamilnadu, 624 622, India.

Department of Mechanical Engineering, Chettinad College of Engineering & Technology, Karur, Tamilnadu, 639114, India.

出版信息

Heliyon. 2019 Jul 29;5(7):e02030. doi: 10.1016/j.heliyon.2019.e02030. eCollection 2019 Jul.

Abstract

Double helically coiled tube heat exchangers are used in different heat transfer utilization due to higher heat transfer capabilities and with their compactness. The double helically coiled tube heat exchanger increases the turbulence and enhances the maximum heat transfer rate than the straight tubes. In this investigation, the heat transfer and pressure drop of the double helically coiled heat exchanger handling MWCNT/water nanofluids have been analyzed by the computational software ANSYS 14.5 version. The computational analysis was carried out under the laminar flow condition in the Dean number range of 1300-2200. The design of new shell and double helically coiled tube heat exchanger was done by using standard designing procedure and 3D modeling was done in Cre-O 2.0 parametric. The Finite Element Analysis software ANSYS Workbench 14.5 was used to perform CFD analysis under the standard working condition. The MWCNT/water nanofluids at 0.2%, 0.4%, and 0.6% volume concentrations have been taken for this investigation. The major factors like volume concentrations of nanofluids and Dean Number are considered for predicting the heat transfer rate and pressure drop. The simulation data was compared with the experimental data. It is studied that the heat transfer rate and pressure drop increase with increasing volume concentrations of MWCNT/water nanofluids. It is found that the Nusselt number of 0.6% MWCNT/water nanofluids is 30% higher than water at the Dean number value of 1400 and Pressure drop is 11% higher than water at the Dean number value of 2200. It is found that the simulation data hold good agreement with the experimental data. The common deviation between the Nusselt number and pressure dropof CFD data and the Nusselt number and pressure drop of experimental data are found to be 7.2% and 8.5% respectively.

摘要

双螺旋盘管式换热器因其较高的传热能力和紧凑性而被应用于不同的传热用途中。与直管相比,双螺旋盘管式换热器增加了流体的湍动程度,并提高了最大传热速率。在本研究中,利用计算软件ANSYS 14.5版本分析了处理多壁碳纳米管/水纳米流体的双螺旋盘管式换热器的传热和压降情况。计算分析是在Dean数范围为1300 - 2200的层流条件下进行的。新的壳程和双螺旋盘管式换热器的设计采用标准设计程序,并在Cre-O 2.0参数化软件中进行三维建模。使用有限元分析软件ANSYS Workbench 14.5在标准工况下进行计算流体动力学(CFD)分析。本研究采用了体积浓度分别为0.2%、0.4%和0.6%的多壁碳纳米管/水纳米流体。在预测传热速率和压降时考虑了纳米流体的体积浓度和Dean数等主要因素。将模拟数据与实验数据进行了比较。研究发现,传热速率和压降随着多壁碳纳米管/水纳米流体体积浓度的增加而增大。发现在Dean数为1400时,体积浓度为0.6%的多壁碳纳米管/水纳米流体的努塞尔数比水高30%,在Dean数为2200时,其压降比水高11%。结果表明,模拟数据与实验数据吻合良好。CFD数据的努塞尔数和压降与实验数据的努塞尔数和压降之间的平均偏差分别为7.2%和8.5%。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/b048/6667788/89f915736b87/gr1.jpg

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