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Numerical study on thermal-hydraulic performance and exergy analysis of laminar oil flow in a circular tube with fluid exchanger inserts

机译:流体交换插入物圆管中流水流动热液压性能和漏洞分析的数值研究

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摘要

A novel tube insert, fluid exchanger inserts, is proposed and numerically investigated for enhancing convective heat transfer of laminar oil flow in a circular tube. Effects of parameters including diameter ratio and number of inserts on convective heat transfer performance are also investigated. In the present work, servotherm medium oil is selected as the working fluid. It is found that the heat transfer performance is effectively enhanced as the thermal boundary layer is completely destroyed when the fluid passes through the fluid exchanger inserts. The Nusselt number and friction factor of the tube with fluid exchanger inserts are enhanced to 1.63-2.69 and 1.72-7.01 times that of the plain tube, respectively. Thus, the performance evaluation criterion ranges from 1.24 to 1.62. Moreover, exergy analysis is conducted to appraise the thermodynamic performance of the tube with fluid exchanger inserts. It is found that the exergy efficiency of the enhanced tube is improved by 0.3%-1.9% compared to the plain tube.
机译:提出了一种新型管插入物,流体交换器插入物,并在数值上研究了用于增强圆管中的层流量的对流传热。还研究了参数的影响,包括直径比和插入件对对流传热性能的影响。在本作工作中,选择Servotherm培养基作为工作流体。发现当流体通过流体交换器插入件时,随着热边界层完全破坏,有效地增强了传热性能。具有流体交换器插入件的管的露珠数和摩擦系数分别增强至普通管的1.63-2.69和1.72-7.01倍。因此,性能评估标准范围为1.24至1.62。此外,进行了Deergy分析以利用流体交换器插入物评估管的热力学性能。结果发现,与平原管相比,增强管的低渗效率提高了0.3%-1.9%。

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