PARAMETRIC EFFECT OF THE INTERRUPTED ANNULAR GROOVE FIN ON FLOW AND HEAT TRANSFER CHARACTERISTICS OF A FINNED CIRCULAR TUBE HEAT EXCHANGER

被引:4
作者
Lin, Zhimin [1 ]
Yang, Ruixia [1 ]
Yang, Haihong [1 ]
Wang, Liangbi [1 ]
Zhang, Yongheng [1 ]
Guo, Anning [1 ]
机构
[1] Lanzhou Jiaotong Univ, Sch Mech Engn, Key Lab Railway Vehicle Thermal Engn, MOE, Lanzhou, Gansu, Peoples R China
来源
THERMAL SCIENCE | 2022年 / 26卷 / 06期
基金
中国国家自然科学基金;
关键词
finned tube heat exchanger; heat transfer augmentation; interrupted annular groove fin; numerical simulation; ABSOLUTE VORTICITY FLUX; VORTEX GENERATORS; BANK FIN; TRANSFER ENHANCEMENT; LOUVERED FIN; MAIN FLOW; PERFORMANCE; VISUALIZATION; PAIR;
D O I
10.2298/TSCI211015040L
中图分类号
O414.1 [热力学];
学科分类号
摘要
The influences of the geometrical parameters of interrupted annular groove fin mainly including the annular groove diameter, the groove arc length, and the fin spacing, on the fin side thermal-hydraulic characteristics of a finned circular tube exchanger were numerically investigated by actualizing the custom FORTRAN programing with SIMPLE algorithm in a non-orthogonal curvilinear co-ordinate system, and the regression formulas of average Nusselt number and friction factor with flow parameters and geometrical parameters were obtained. Compared with the referential plain fin, interrupted annular groove fin could significantly improve thermal performance under the same pumping power constraint, and Nusselt number is closely germane to the secondary flow, which implies that the fin side heat transfer is depended entirely on the secondary flow strength. For Nusselt number, the annular groove diameter and the groove arc length have positive effect, while the fin pitch, the groove circumferential and radial locations have negative effect. The dominant parameters influencing on friction factor in turn are the fin pitch, the groove radial location, and the annular groove diameter. The optimal annular groove diameter is screened, and found that the optimal annular groove diameter is closely related with Reynolds number under the same pumping power constraint, while under the same mass-flow rate constraint that is scarcely related with Reynolds number.
引用
收藏
页码:4503 / 4517
页数:15
相关论文
共 31 条
[1]   Effect of a delta-winglet vortex pair on the performance of a tube-fin heat exchanger [J].
Allison, C. B. ;
Dally, B. B. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2007, 50 (25-26) :5065-5072
[2]   MULTI-SURFACE METHOD OF COORDINATE GENERATION [J].
EISEMAN, PR .
JOURNAL OF COMPUTATIONAL PHYSICS, 1979, 33 (01) :118-150
[3]   PRACTICAL 3-DIMENSIONAL MESH GENERATION USING TRANSFINITE INTERPOLATION [J].
ERIKSSON, LE .
SIAM JOURNAL ON SCIENTIFIC AND STATISTICAL COMPUTING, 1985, 6 (03) :712-741
[4]   Heat transfer characteristics of a circular tube bank fin heat exchanger with fins punched curve rectangular vortex generators in the wake regions of the tubes [J].
Gong, Bao ;
Wang, Liang-Bi ;
Lin, Zhi-Min .
APPLIED THERMAL ENGINEERING, 2015, 75 :224-238
[5]   Analysis of heat transfer and pressure drop for fin-and-tube heat exchangers with rectangular winglet-type vortex generators [J].
He, Ya-Ling ;
Chu, Pan ;
Tao, Wen-Quan ;
Zhang, Yu-Wen ;
Xie, Tao .
APPLIED THERMAL ENGINEERING, 2013, 61 (02) :770-783
[6]   Performance enhancement of a louvered fin heat exchanger by using delta winglet vortex generators [J].
Huisseune, Henk ;
T'Joen, Christophe ;
De Jaeger, Peter ;
Ameel, Bernd ;
De Schampheleire, Sven ;
De Paepe, Michel .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2013, 56 (1-2) :475-487
[7]  
Jiang G. D., 2000, J CHEM IND ENG, V51, P604
[8]   Heat transfer and fluid flow analysis in plate-fin and tube heat exchangers with a pair of block shape vortex generators [J].
Leu, JS ;
Wu, YH ;
Jang, HY .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2004, 47 (19-20) :4327-4338
[9]   Experimental and numerical study and comparison of performance for wavy fin and a plain fin with radiantly arranged winglets around each tube in fin-and-tube heat exchangers [J].
Li, M. J. ;
Zhang, H. ;
Zhang, J. ;
Mu, Y. T. ;
Tian, E. ;
Dan, D. ;
Zhang, X. D. ;
Tao, W. Q. .
APPLIED THERMAL ENGINEERING, 2018, 133 :298-307
[10]   A new stability-guaranteed second-order difference scheme [J].
Li, ZY ;
Tao, WQ .
NUMERICAL HEAT TRANSFER PART B-FUNDAMENTALS, 2002, 42 (04) :349-365