Numerical investigation of flow and heat transfer performances of horizontal spiral-coil pipes

被引:23
|
作者
Ji, Jia-dong [1 ]
Ge, Pei-qi [1 ,2 ]
Bi, Wen-bo [1 ]
机构
[1] Shandong Univ, Sch Mech Engn, Jinan 250061, Peoples R China
[2] Shandong Univ, Minist Educ, Key Lab High Efficiency & Clean Mech Manufacture, Jinan 250061, Peoples R China
基金
中国国家自然科学基金;
关键词
heat exchanger; horizontal spiral-coil pipe; heat transfer performance; flow performance; secondary fluid flow; CONSTANT WALL TEMPERATURE; WET-SURFACE CONDITIONS; TRANSFER COEFFICIENTS; DRY-SURFACE; TUBE; EXCHANGERS; CURVATURE; SHELL;
D O I
10.1016/S1001-6058(16)60661-3
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
The flow and heat transfer performances of horizontal spiral-coil pipes of circular and elliptical cross-sections are studied. The numerical results are compared with the experimental data, to verify the numerical method. The effects of the inlet water mass flow rate, the structural parameters, the helical pitch and the radius ratio on the heat transfer performances are investigated. Performances of the secondary fluid flow with different radius ratios are also investigated. Numerical results demonstrate that the heat transfer coefficient and the Nusselt number increase with the increase of the water mass flow rate or the helical pitch. The maximum heat transfer coefficient and the maximum Nusselt number are obtained when the radius ratio is equal to 1.00. In addition, the fluid particle moves spirally along the pipe and the velocity changes periodically. The particle flow intensity and the spiral movement frequency decrease significantly with the increase of the radius ratio. Besides, the secondary flow profile in the horizontal spiral-coil pipe contains two oppositely rotating eddies, and the eddy intensity decreases significantly along the pipe owing to the change of curvature. The decreasing tendency of the eddy intensity along the pipe increases with the increase of the radius ratio.
引用
收藏
页码:576 / 584
页数:9
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