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Heat transfer and performance analysis of nanofluid flow in helically coiled tube heat exchangers

机译:螺旋盘管换热器中纳米流体流动的传热和性能分析

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In the present paper, heat transfer characteristics of Al2O3 nanofluid flow inside shell and helical tube heat exchangers are numerically investigated. The numerical computations are performed by using SST turbulence model as well as by implementing conjugate heat transfer from hot fluid in the tube to cold fluid in the shell. The thermo-physical properties of the fluids were considered to be temperature dependent. The coil-side Reynolds number, the shell-side Reynolds number and the Prandtl number ranged between 9000 and 36,000, 600 and 2600 and 2.2 and 8.3, respectively. The effects of nanoparticle volume concentration on the temperature of coil- and shell-side flows, heat transfer rate and convective heat transfer coefficients are presented. The results indicate that the presence of 0.2% and 0.3% nanoparticle volume concentration increases the mean heat transfer rate by approximately 14% and 18%, respectively. The results also show that with the increase in particle volume concentration the coil-side, shell-side and overall heat transfer coefficients enhance. It is indicated that for the same mass flow rate, the heat transfer rate of nanofluid enhances noticeably compared to water and it increases marginally with the further increase in the nanoparticle volume concentration. The performance of the heat exchanger was evaluated and the results reveal that the effectiveness enhances by decreasing the mass flow rate and increasing the particle volume concentration, tube diameter and coil diameter. Moreover, the performance index enhances by increasing the tube diameter and reducing the coil diameter. (C) 2016 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:本文研究了Al2O3纳米流体在壳内和螺旋管式换热器内部流动的传热特性。通过使用SST湍流模型以及通过实现从管中的热流体到壳中的冷流体的共轭传热来执行数值计算。流体的热物理性质被认为是温度依赖性的。线圈侧雷诺数,壳侧雷诺数和普朗特数分别在9000和36,000之间,600和2600之间以及2.2和8.3之间。提出了纳米颗粒体积浓度对盘管和壳侧流动温度,传热速率和对流传热系数的影响。结果表明,存在0.2%和0.3%的纳米颗粒体积浓度分别使平均传热率分别增加约14%和18%。结果还表明,随着颗粒体积浓度的增加,盘管侧,壳侧和总传热系数均增加。已经表明,对于相同的质量流量,与水相比,纳米流体的传热速率显着提高,并且随着纳米颗粒体积浓度的进一步增加,其略微增加。对热交换器的性能进行了评估,结果表明,通过降低质量流量和增加颗粒体积浓度,管径和盘管直径,可以提高效率。此外,通过增加管直径和减小线圈直径来提高性能指标。 (C)2016化学工程师学会。由Elsevier B.V.发布。保留所有权利。

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