Experimental study of thermo-hydraulic and fouling performance of enhanced heat exchangers

被引:16
作者
Pahlavanzadeh, H.
Nasr, M. R. Jafari
Mozaffari, S. H.
机构
[1] Tabait Modares Univ, Dept Chem Engn, Tehran, Iran
[2] Res & Technol Petrochem Co, Tehran, Iran
关键词
tube insert; heat transfer enhancement; fouling mitigation; pressure drop; friction factor; wire coil; wire mesh;
D O I
10.1016/j.icheatmasstransfer.2007.04.002
中图分类号
O414.1 [热力学];
学科分类号
摘要
The present study investigated the effect of two tube inserts (wire coil and wire mesh) on the heat transfer enhancement, pressure drop and mineral salts fouling mitigation in tube of a heat exchanger. A 3/4-in. tube that is heated by band heaters, is used which simulated a tube of heat exchanger. Working fluid is water with certain quality. The heat transfer rate averagely increased by 22-28% for wire coil (pld=0.125, eld=0.00375) and 163-174% for wire mesh (medium density) over a plain tube value, depending on type of tube insert, density of wire torsion and flow velocity. However, the pressure drop also increased substantially by 46% for wire coil and 500% for wire mesh. Wire coil insert with vibration mitigate mineral salts fouling (scaling) about 34%, and wire mesh have no effect on scaling, however it sometimes increased deposit rate. (C) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:907 / 916
页数:10
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