Investigation of the semi-dimple vortex generator applicable to fin-and-tube heat exchangers

被引:34
作者
Wang, Chi-Chuan [1 ]
Chen, Kuan-Yu [1 ]
Lin, Yur-Tsai [2 ]
机构
[1] Natl Chiao Tung Univ, Dept Mech Engn, Hsinchu 300, Taiwan
[2] Yuan Ze Univ, Dept Mech Engn, Taoyuan, Taiwan
关键词
Fin-and-tube heat exchanger; Semi-dimple; Vortex generator; Heat transfer; TRANSFER ENHANCEMENT; PLATE-FIN; RECENT PATENTS; PERFORMANCE; FLOW; VORTICES; ROWS;
D O I
10.1016/j.applthermaleng.2014.09.054
中图分类号
O414.1 [热力学];
学科分类号
摘要
The present study examines the air side performance of the fin-and-tube heat exchangers having semi-dimple vortex generator or plain fin geometry. A total of eight samples are made and tested with the corresponding fin pitch (F-P) being 1.6 mm and 2.0 mm and the number of tube row (N) are 1 and 2. The inlet air flow direction is also being tested upon the proposed semi-dimple VG. Test results indicate that the heat transfer performance of the proposed semi-dimple VG with N = 1 at a smaller fin pitch of 1.6 mm is slightly higher than that of plain fin geometry. For N = 1 with a larger fin pitch of 2.0 mm, the semi-dimple VG is about 10% higher than that of plain fin geometry. The difference in heat transfer performance amid VG and plain fin geometry becomes more pronounced with N = 2 and is especially evident when F-P = 2.0 mm due to mixing contribution. In general, the difference between plain and semi-dimple geometry becomes more conspicuous at a larger fin pitch because of the comparatively effectively swirled motion. Both geometries show a dependence on fin pitch at N = 1 but the effect is almost negligible when N is increased to 2. The inlet air flow direction casts negligible influence on the heat transfer performance of semi-dimple VG. However, the friction factors for the opposite air flow operation is lower than that of normal operation, especially in low Reynolds number region. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:192 / 197
页数:6
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