2018
DOI: 10.1016/j.ijheatmasstransfer.2018.04.071
|View full text |Cite
|
Sign up to set email alerts
|

Effect of winglet location on performance of fin-tube heat exchangers with inline tube arrangement

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
12
0
2

Year Published

2018
2018
2024
2024

Publication Types

Select...
5
3

Relationship

0
8

Authors

Journals

citations
Cited by 44 publications
(14 citation statements)
references
References 36 publications
0
12
0
2
Order By: Relevance
“…However, the swirl flow (longitudinal vortices) generated by a pair of VGs was found to weaken in the downstream direction. The longitudinal vortices could not last long under the recirculation effect of the flow behind the tube [9]. This problem was solved by adding VG pairs.…”
Section: Velocity Streamline and Vectormentioning
confidence: 99%
See 1 more Smart Citation
“…However, the swirl flow (longitudinal vortices) generated by a pair of VGs was found to weaken in the downstream direction. The longitudinal vortices could not last long under the recirculation effect of the flow behind the tube [9]. This problem was solved by adding VG pairs.…”
Section: Velocity Streamline and Vectormentioning
confidence: 99%
“…Many scholars have tried to increase the convective heat transfer coefficient using a VG. Through three-dimensional (3D) modeling, Naik and Tiwari [9] studied the effect of winglet locations on heat transfer features in fin and tube heat exchangers using inline RWPs, and observed that the Nusselt number (Nu) and secondary flow intensity (Se) peaked at ∆Y = ± 1.25 and attack angle (β) = 45°, which are mounted in the downstream area adjacent to the tube. Lu and Zhai [10] numerically analyzed the heat transfer and pressure drop on a fin and oval tube heat exchanger using a tear-drop delta VG, found that the tear-drop delta GV outperforms plain delta VG, and investigated the mechanism of the advantage in the light of Se and field synergy principle.…”
Section: Introductionmentioning
confidence: 99%
“…An obvious difference in Nu s exists between c 4 and c 7 . Since the common flow region is beneficial to heat transfer [17], the local value of Nu s generally increases in the short region behind the winglets, and the region length with a large value of Nu s decreases, with c changing from c 4 to c 6 . This is because the interaction between the vortices increases with c changing from c 4 to c 6 , and the intensity of the vortices attenuates rapidly in the downstream region.…”
Section: Distributions Of the Span-average Values Of Se S And Nu Smentioning
confidence: 99%
“…[16] experimentally studied a fin with radiantly arranged VGs and showed that the fin with the radiantly-arranged VGs had a better 2 of 14 comprehensive performance than the studied wavy fin. Naik and Tiwari [17] studied the location of VGs in the CFD configuration and reported that heat transfer is the highest for the VGs located in the adjacent region.…”
Section: Introductionmentioning
confidence: 99%
“…It should be noted that this principle is frequently considered in industrial heat exchanger designs using various shapes, such as fin, baffle, vortex generator and so forth, to increase heat transfer efficiency [25][26][27][28][29][30][31][32][33][34]. The key point in this heat exchanger design is to take into consideration both the negative aspect of increased flow resistance that arises from the installation of the obstacle and the positive aspect of heat transfer enhancement to the vortex as mentioned above.…”
Section: Introductionmentioning
confidence: 99%