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

机译:处理MWCNT /水纳米流体的双螺旋螺旋管式换热器热流特性的CFD分析

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摘要

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.
机译:双螺旋盘管式换热器由于具有更高的传热能力和紧凑性,因此用于不同的传热利用中。与直管相比,双螺旋盘管式换热器增加了湍流并提高了最大传热速率。在这项研究中,通过计算软件ANSYS 14.5版本分析了处理MWCNT /水纳米流体的双螺旋盘绕热交换器的传热和压降。计算分析是在层流条件下,迪安数在1300-2200范围内进行的。使用标准设计程序完成了新壳体和双螺旋盘管换热器的设计,并在Cre-O 2.0参数中完成了3D建模。使用有限元分析软件ANSYS Workbench 14.5在标准工作条件下执行CFD分析。这项研究采用了0.2%,0.4%和0.6%体积浓度的MWCNT /水纳米流体。考虑诸如纳米流体的体积浓度和迪安数的主要因素来预测传热速率和压降。将模拟数据与实验数据进行比较。研究表明,传热速率和压降随着MWCNT /水纳米流体体积浓度的增加而增加。发现当Dean值为1400时,0.6%MWCNT /水纳米流体的Nusselt值比水高30%,当Dean值为2200时,压降比水高11%。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共同偏差分别为7.2%和8.5%。

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