Yong Luan

Dr. Yong Luan


Research Focus & Metrics

Academic Career Length

5Years (2022-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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25 February 2022 in Journal of Turbomachinery
Verified
Journal Article
Closed access
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YLYong Luan
Yong Luan
Yu RaoYu Rao
Yu Rao
KWKai Wang
Kai Wang
WWWeilong Wu
Weilong Wu

20 January 2023 in Energies
Verified
Journal Article
Open access
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YLYuyang Liu
Yuyang Liu
YLYong Luan
Yong Luan
XDXinbo Dai
Xinbo Dai
SLSenyun Liu
Senyun Liu
XYXian Yi
Xian Yi
Yu RaoYu Rao
Yu Rao
Swirling hot air is a promising heat transfer enhancement technology for anti-icing applications in aircrafts, where the swirling flow is accompanied by pretty high turbulence and a quite thin boundary layer. It is of interest to investigate the compound heat transfer characteristics of the swirling air configuration combined with surface structures on the internal wall. This paper carries out a series of numerical computations to obtain the Nusselt number and pressure loss data in such a swirling air heat transfer system with four kinds of surface structures (trenches, ribs, dimples and bulges) on the wall and with different tangential inlet jets placed along the tube. At a tube Reynolds number from 10,000 to 50,000, the results show that the surface dimples and bulges are conducive to improving the Nusselt number, but the surface trenches and ribs show a Nusselt number deterioration relative to the smooth swirl tube. Among the four investigated surface structures, the surface bulges perform best, which can enhance the Nusselt number by up to 15.0%, increase the total heat transfer quantity by up to 17.3% and reduce the hot air pressure loss by up to 15.6%. Furthermore, the circumferential velocity distribution and swirl number are introduced to describe the flow fields. The surface trenches and ribs lead to less of a reduction in the circumferential velocity and swirl intensity, while the surface dimples and bulges could significantly suppress the in-tube swirl intensity.

6 February 2025 in ASME Journal of Heat and Mass Transfer
Verified
Journal Article
Closed access
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CXChao Xu
Chao Xu
JCJianian Chen
Jianian Chen
Yu RaoYu Rao
Yu Rao
YLYong Luan
Yong Luan
Heat transfer and pressure loss characteristics of a novel Vortex rib in a cooling channel have been studied both experimentally and numerically under the Reynolds numbers from 10,000 to 80,000 and rotation numbers from 0 to 0.385. The Vortex rib is proposed by combining W-rib and W-patterned oblong dimple. Compared with the W-rib, the Vortex rib enhances heat transfer by up to 11.4% (Re = 10,000 and Ro = 0.31) while reducing the pressure loss by up to 18.7% (Re = 32,000 and Ro = 0) under non-rotating and rotating conditions. Compared to the W-patterned oblong dimple, the heat transfer of the Vortex rib increases by up to 47.9%. The heat transfer dead zones are significantly improved by near-wall vortex induced by Vortex rib. The Vortex rib can appreciably reduce the turbulent mixing intensity in the mainstream of the cooling fluid but keep the near-wall high turbulent mixing intensity, guaranteeing the turbulent heat transport capacity. Thus, the heat transfer can be improved while maintaining the pressure loss in the channel.

18 October 2023 in ASME Journal of Heat and Mass Transfer
Verified
Journal Article
Closed access
PDF file
FLFei Li
Fei Li
CXChenglan Xiong
Chenglan Xiong
Yu RaoYu Rao
Yu Rao
YLYong Luan
Yong Luan
BWBernhard Weigand
Bernhard Weigand
The paper presents a numerical study of the heat transfer, pressure loss and flow characteristics of swirl cooling in elliptical tubes, which are compared to the counterpart of swirl cooling in a circular tube with a diameter of D=50.0 mm under equal passage Reynolds numbers and equal jet Reynolds numbers. The swirl tubes with two kinds of fixed tube length of 12D and 20D are compared, where there are sequentially arranged three tangential jet inlets over the leading tube length of 12D. The numerical results show that the swirl tubes with the tube length of 12D has a much better heat transfer performance. Under equal passage Reynolds numbers, the elliptical swirl tubes with the tube length of 12D show appreciably higher Nusselt numbers by up to 22.8% and lower pressure loss coefficients by up to 69.0% than the circular tube. Under equal jet Reynolds numbers, the elliptical tubes can reduce the global heat transfer performance modestly by up to 25.6%, but reduce the pressure loss much significantly by up to 70.6%. Mostly due to much less pressure loss, the elliptical tubes have remarkably higher thermal performance in terms of the obtained heat transfer coefficient per unit pumping power for both L1=12D and L2=20D. The numerical simulations indicate that the suppression of elliptical tubes on the swirling flow development reduces the heat transfer on the wall between the jet inlets, and decreases the wall shear force and the pressure loss in the tube.