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Heat transfer, friction factor and effectiveness analysis of Fe_3O_4/water nanofluid flow in a double pipe heat exchanger with return bend

机译:Fe_3O_4 /水纳米流回弯双管换热器的传热,摩擦系数及有效性分析

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摘要

The convective heat transfer, friction factor and effectiveness of different volume concentrations nanofluid flow in an inner tube of double pipe heat exchanger with return bend has been estimated experimentally and turbulent flow conditions. The test section used in this study is of double pipe type in which the inner tube diameter is 0.019 m, the annulus tube diameter is 0.05 m and the total length of inner tube is 5 m. At a distance of 2.2 m from the inlet of the inner tube the return bend is provided. The hot Fe_3O_4 nanofluid flows through an inner tube, where as the cold water flows through an annulus tube. The volume concentrations of the nano-particles used in this study are 0.005%, 0.01%, 0.03% and 0.06% with Reynolds number range from 15,000 to 30,000. Based on the results, the Nusselt number enhancement is 14.7% for 0.06% volume concentration of nanofluid flow in an inner tube of heat exchanger at a Reynolds number of 30,000 when compared to base fluid data; the pumping penalty of nanofluid is < 10%. The effectiveness of heat exchanger for water and nanofluid flow is explained in terms of number of transfer units (NTU) in order to estimate the overall performance of the double pipe heat exchanger. New correlations for Nusselt number and friction factor have been developed based on the experimental data.
机译:通过实验和湍流条件,估算了不同体积浓度的纳米流体在具有弯折的双管换热器内管中的对流传热,摩擦系数和有效性。本研究中使用的测试段为双管型,内管直径为0.019 m,环管直径为0.05 m,内管总长度为5 m。在距内管入口2.2 m处设有回弯管。热的Fe_3O_4纳米流体流经内管,而冷水流经环形管。本研究中使用的纳米粒子的体积浓度为0.005%,0.01%,0.03%和0.06%,雷诺数范围为15,000至30,000。根据结果​​,与基础流体数据相比,当换热器内管中的纳米流体流量为0.06%时,努氏数提高了14.7%,雷诺数为30,000。纳米流体的抽运罚款<10%。为了估计双管式换热器的整体性能,用传热单元(NTU)的数量来说明换热器对水和纳米流体流动的有效性。基于实验数据,已开发出Nusselt数和摩擦系数的新相关性。

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