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HEAT TRANSFER ENHANCEMENT AND PRESSURE DROP OF GROOVED ANNULUS OF DOUBLE PIPE HEAT EXCHANGER

机译:双管换热器沟槽环的传热增强和压降

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摘要

This investigation was performed to experimentally investigate the enhancement of heat transfer and the friction of an annulus in a double pipe heat exchanger system with rectangular grooves in the turbulent flow regime. The shell is made of acrylic and its diameter is 28 mm. The tube is made of aluminium and its diameter is 20 mm. Grooves were incised in the annulus room with a circumferential pattern, with a groove space of 2 mm, a distance between the grooves of 8mm and a groove height of 0.3 mm. The experiments consist of temperature and pressure measurement and a flow visualization. Throughout the investigation, the cold fluid flowed in the annulus room. The Reynold number of cold fluid varied from about 31981 to 43601 in a counter flow condition. The volume flow rate of hot fluid remains constant with Reynold number about 30904. Result showed the effect of grooves, which are applied in the annulus room. The grooves induce the pressure drop, the pressure drop in the grooved annulus was greater by about 15.88% to 16.72% than the one in the smooth annulus. The total heat transfer enhancement is of 1.09–1.11. Moreover, the use of grooves in the annulus of the heat exchanger not only increase the heat transfer process, but also increase the pressure drop, which is related to the friction factor.
机译:进行这项研究是为了实验研究在湍流状态下具有矩形凹槽的双管热交换器系统中传热的增强和环空的摩擦。外壳由丙烯酸制成,直径为28毫米。该管由铝制成,直径为20毫米。在环形室中以圆周图案切出凹槽,凹槽空间为2mm,凹槽之间的距离为8mm,凹槽高度为0.3mm。实验包括温度和压力测量以及流量可视化。在整个调查过程中,冷流体在环室中流动。在逆流条件下,冷流体的雷诺数从31981到43601不等。热流体的体积流率保持恒定,雷诺数约为30904。结果显示了在环室中使用沟槽的效果。凹槽引起压降,凹槽环中的压降比光滑环中的压降大约15.88%至16.72%。总传热增强为1.09–1.11。此外,在热交换器的环形空间中使用凹槽不仅增加了传热过程,而且还增加了与摩擦系数有关的压降。

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