Performance Optimization of the Helical Heat Exchanger With Turbulator

被引:14
|
作者
Xifeng, Wang [1 ]
Xiaoluan, Zhang [1 ]
Mahariq, Ibrahim [2 ]
Salem, Mohamed [3 ]
Ghalandari, Mohammad [4 ]
Ghadak, Farhad [5 ]
Abedini, Mostafa [6 ]
机构
[1] Baoji Univ Arts & Sci, Sch Comp Sci, Baoji, Peoples R China
[2] Amer Univ Middle East, Coll Engn & Technol, Egaila, Kuwait
[3] Univ Sains Malaysia USM, Sch Elect & Elect Engn, Nibong Tebal, Malaysia
[4] Duy Tan Univ, Inst Res & Dev, Da Nang, Vietnam
[5] Sharif Univ Technol, Dept Aerosp Engn, Tehran, Iran
[6] KN Toosi Univ Technol, Fac Mech Engn, Tehran, Iran
关键词
helical heat exchanger; fins effects; heat transfer; pressure loss; multi-disciplinary design optimization method; TRANSFER ENHANCEMENT; PRESSURE-DROP; FLUID; SHELL; FLOW; NANOFLUID; BOUNDS; MODEL; PIPE;
D O I
10.3389/fenrg.2021.789316
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this paper, optimization on a two-tube helical heat exchanger with a fin is represented. The spiral pipes heat exchanger which is made of the cooper is adopted for investigation. The effects of three types of fins with the proposed geometric shapes on the overall heat transfer coefficient and pressure loss are investigated. The fins are located on the inner surface of the outer pipe. The obtained numerical results are compared with the experimental results, and a good agreement is observed between the results. The studies show that the total heat transfer coefficient has increased by 170% compared to an exchanger with no fin. Therefore, the best fin has been selected based on the benefit-cost-ratio (BCR) factor. Finally, using the new represented optimization algorithm, the height of the represented triangular fin is optimized to represent the best values for overall heat transfer coefficient and pressure loss of the helical heat exchanger. In addition, the results indicate that reducing the density and height of the triangular fin increases heat transfer and reduces pressure loss.
引用
收藏
页数:11
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