OPTIMIZATION OF THE LOUVER FIN-AND-TUBE HEAT EXCHANGERS-A PARAMETRIC APPROACH

被引:19
作者
Sadeghianjahromi, Ali [1 ]
Kheradmand, Saeid [2 ]
Nemati, Hossain [3 ]
Wang, Chi-Chuan [1 ]
机构
[1] Natl Chiao Tung Univ, Dept Mech Engn, 1001 Univ Rd, Hsinchu 300, Taiwan
[2] Malek Ashtar Univ Technol, Dept Mech & Aerosp Engn, POB 83145-115, Esfahan, Iran
[3] Islamic Azad Univ, Dept Mech, Marvdasht Branch, Marvdasht, Iran
关键词
heat transfer enhancement; louver fin-and-tube heat exchanger; louver angle; fin pitch; tube pitch; numerical simulation; AIR-SIDE PERFORMANCE; THERMAL-HYDRAULIC PERFORMANCE; PLATE-FIN; FRICTION CHARACTERISTICS; PRESSURE-DROP; FLAT-TUBE; FLOW VISUALIZATION; WAFFLE HEIGHT; FLUID-FLOW; OVAL;
D O I
10.1615/JEnhHeatTransf.2020033527
中图分类号
O414.1 [热力学];
学科分类号
摘要
3D turbulent flow numerical simulations are performed to study heat transfer and flow friction characteristics of louver fin-and-tube heat exchangers. The effects of louver angle, fin pitch, transversal tube pitch, and longitudinal tube pitch on Colburn and friction factors are investigated in detail. Three stages of the effect of louver angle on the Colburn j factor are identified, including rising, level-off, and increasing again. A wide range for louver angle ranging from 0 degrees (plain fin) to 80 degrees is considered. Results show that the Colburn factor increases from a louver angle of 0 degrees (plain fin) to 20 degrees, followed by a level-off or slight decline until the louver angle reaches 45 degrees, and finally, the Colburn factor is increased again with a further rise of louver angle. However, the friction factor increases with an increase in louver angle from 0 degrees (plain fin) to 80 degrees. Colburn and friction factors are almost independent of fin pitch while they decrease with an increase in transversal and longitudinal tube pitches. The optimum louver angle is around 20 degrees upon carrying out the full factorial method in maximizing Colburn factor and minimizing friction factor.
引用
收藏
页码:289 / 312
页数:24
相关论文
共 54 条
  • [1] HEAT-TRANSFER AND PRESSURE-DROP CHARACTERISTICS OF FLAT TUBE AND LOUVERED PLATE FIN SURFACES
    ACHAICHIA, A
    COWELL, TA
    [J]. EXPERIMENTAL THERMAL AND FLUID SCIENCE, 1988, 1 (02) : 147 - 157
  • [2] [Anonymous], 2014, CFD LETT
  • [3] Constructal Optimization of Louver Fin Channels Subjected to Heat Transfer Rate Maximization and Pressure Loss Minimization
    Asadi, Masoud
    Sunden, Bengt
    Xie, Gongnan
    [J]. HEAT TRANSFER ENGINEERING, 2018, 39 (05) : 436 - 448
  • [4] Two- and three-dimensional numerical models of flow and heat transfer over louvred fin arrays in compact heat exchangers
    Atkinson, KN
    Drakulic, R
    Heikal, MR
    Cowell, TA
    [J]. INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1998, 41 (24) : 4063 - +
  • [5] MODELS FOR PRESSURE DROP AND HEAT TRANSFER IN AIR COOLED COMPACT WAVY FIN HEAT EXCHANGERS
    Awad, M. M.
    Muzychka, Y. S.
    [J]. JOURNAL OF ENHANCED HEAT TRANSFER, 2011, 18 (03) : 191 - 207
  • [6] Baldwin S. P., 1987, P 5 INT C NUM METH L, P482
  • [7] Heat transfer analysis of fin-and-tube heat exchangers with flat and louvered fin geometries
    Carija, Zoran
    Frankovic, Bernard
    Percic, Marko
    Cavrak, Marko
    [J]. INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2014, 45 : 160 - 167
  • [8] Cavazzuti Marco, 2013, Optimization Methods From Theory to Design Scientific and Technological Aspects in Mechanics
  • [9] FLOW AND HEAT-TRANSFER IN COMPACT LOUVERED FIN SURFACES
    COWELL, TA
    HEIKAL, MR
    ACHAICHIA, A
    [J]. EXPERIMENTAL THERMAL AND FLUID SCIENCE, 1995, 10 (02) : 192 - 199
  • [10] A Comparison of Metal-Foam Heat Exchangers to Compact Multilouver Designs for Air-Side Heat Transfer Applications
    Dai, Z.
    Nawaz, K.
    Park, Y.
    Chen, Q.
    Jacobi, A. M.
    [J]. HEAT TRANSFER ENGINEERING, 2012, 33 (01) : 21 - 30