Laminar heat transfer performance of power law fluids in coiled square tube with various configurations

被引:26
作者
Kurnia, Jundika C. [1 ]
Sasmito, Agus P. [2 ]
Mujumdar, Arun S. [2 ]
机构
[1] Masdar Inst Sci & Technol, Abu Dhabi, U Arab Emirates
[2] McGill Univ, Dept Min & Mat Engn, Montreal, PQ H3A 2A7, Canada
关键词
Coil; Figure of Merit; Heat transfer performance; Power law; Non-Newtonian; SPIRAL DUCTS; FLOW; EXCHANGER; MODEL; WATER;
D O I
10.1016/j.icheatmasstransfer.2014.07.016
中图分类号
O414.1 [热力学];
学科分类号
摘要
This study addresses heat transfer performance of laminar non-Newtonian fluid flow in various configurations of coiled square tubes e.g., in-plane spiral ducts, helical spiral ducts and conical spiral ducts. The non-Newtonian fluid considered in this study is the aqueous solution of carboxymethyl cellulose (CMC) which is modeled as power-law fluid. Effects of tube geometries, power-law index (concentration of CMC) and other parameters are quantified and discussed to analyze flow behavior and heat transfer performance. Results are compared with those for a straight square tube of the same length as that used to form the coils. A Figure of Merit is defined to compare the heat transfer performance of different geometries with respect to the pumping power. The results suggest that CMC solution yields better heat transfer performance of about twice than that of water at Re similar to 1000. Among all considered designs, helical coil gives the best heat transfer performance; however, when the pumping power is considered, in-plane coil design performs the best in term of Figure of Merit. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:100 / 108
页数:9
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