RESEARCH ARTICLE

A new performance evaluation method and its application in fin-tube surface design of small diameter tube

  • Jufang FAN 1 ,
  • Weikun DING 1 ,
  • Zhigeng WU 1 ,
  • Yaling HE 1 ,
  • Wenquan TAO , 1 ,
  • Yongxin ZHENG 2 ,
  • Yifeng GAO 2 ,
  • Ji SONG 2
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  • 1. School of Energy & Power Engineering, Xi’an Jiaotong University, Xi’an 710049, China
  • 2. International Copper Association Ltd. China, Shanghai Office, Shanghai 200020, China

Received date: 18 Aug 2010

Accepted date: 29 Oct 2010

Published date: 05 Mar 2011

Copyright

2014 Higher Education Press and Springer-Verlag Berlin Heidelberg

Abstract

In this paper, a simple yet efficient performance comparison method is proposed based on the assumptions of constant properties and identical frontal area. For this method, no correlations are required, and a small number of discrete data are sufficient. To illustrate the feasibility of the proposed approach, a new slotted fin with 4 mm tubes is designed to replace the original louvered fin with tubes of 7 mm. The orthogonal design method is adopted in the fin design to reduce the number of computational cases significantly, and yet a nearly optimum combination of major geometric factors can still be obtained. The reasonable parametric combination of 3 global parameters is obtained by analyzing the numerical results of 16 plain plate fins. Based on this result, 3 new slotted fins with different fin pitches are studied. The slotted fin with a fin pitch of 1.4 mm is recommended after considering the heat transfer, comprehensive performance, and cost of material and operation. The result shows that compared with the original louvered fin, the recommended fin not only increases the heat transfer rate by 2.2%, 22.5%, and 13.7% under an identical flow rate, identical pressure drop, and identical pumping power constraint, respectively, but also saves approximately 36% of the copper tube materials.

Cite this article

Jufang FAN , Weikun DING , Zhigeng WU , Yaling HE , Wenquan TAO , Yongxin ZHENG , Yifeng GAO , Ji SONG . A new performance evaluation method and its application in fin-tube surface design of small diameter tube[J]. Frontiers in Energy, 2011 , 5(1) : 59 -68 . DOI: 10.1007/s11708-010-0132-8

Acknowledgements

This work was supported by the National Basic Research Program of China (No. 2007CB206902). The computations were conducted at Xi’an Node of National High-Performance Computing Cluster of China.
Notation
Acfrontal cross-section area/m2
cpspecific heat/(kJ·kg-1·K-1)
Lorthogonal array or straight line
ppressure/Pa
Ppumping power/W
Ttemperature/K
u, v, wvelocity component in Cartesian coordinates system/(m·s-1)
uivelocity component in Cartesian coordinates system/(m·s-1)
Vinlet velocity of fluid/(m·s-1)
x, y, zcoordinate component in Cartesian coordinates system
xicoordinate component in Cartesian coordinates system
Greek symbols
Δpfluid pressure drop between inlet and outlet/Pa
ΔTfluid temperature difference between inlet and outlet/K
Φheat transfer rate/W
ηdynamic viscosity/(kg·m-1·s-1)
λthermal conductivity of fluid/(W·m-1·K-1)
ρfluid density/(kg·m-1)
Subscripts
1,2code for fin for comparison
a, b, ccode for straight line
isummation Indicators
kfree Indicators
wtube wall
1
Webb R L, Kim N H. Principles of Enhanced Heat Transfer. 2nd ed. Boca Raton: Taylor &Francis, 2005

2
Bergles A E. Heat transfer enhancement-The maturing of second-generation heat transfer technology. Heat Transfer Engineering, 1997, 18(1): 47-55

DOI

3
Wang C C. Technology review-A survey of recent patents of fin-and-tube heat exchangers. Enhanced Heat Transfer, 2000, 7(5): 333-345

4
Shah R K, Pekulic D P. Fundamentals of Heat Exchanger Design. Hobokin, New Jersey: John Wiley & Sons, 2003, 696

DOI

5
Wang L B, Tao W Q. Heat transfer and fluid flow characteristics of plate array aligned at angles to the flow direction. International Journal of Heat and Mass Transfer, 1995, 38(16): 3053-3063

DOI

6
Webb R L, Eckert E R. Application of rough surfaces to heat exchanger design. International Journal of Heat and Mass transfer, 1972, 15(9): 1647-1658

DOI

7
Bergles A E. Techniques to enhance heat transfer. In: Rohsenow W M, Hartnett J P, Cho Y L, eds. Handbook of Heat Transfer. 3rd ed. New York: McGraw-Hill, 1998, Chapter 11

8
Sparrow E M, Tao W Q. Symmetric vs asymmetric periodic disturbances at the walls of a heated flow passage. International Journal of Heat and Mass transfer, 1984, 27(11): 2133-2144

DOI

9
Huang H Z, Tao W Q. An experimental study on heat/mass transfer and pressure drop characteristics for arrays of nonuniform plate length positioned obliquely to the flow direction. ASME Journal of Heat Transfer, 1993, 115(3): 568-575

DOI

10
Lue S S, Huang H Z, Tao W Q. Experimental study on heat transfer and pressure drop characteristics in the developing region for arrays of obliquely positioned plates of nonuniform length. Experimental Thermal and Fluid Science, 1993, 7(1): 30-38

DOI

11
Yuan Z X, Tao W Q, Wang Q W. Numerical prediction for laminar forced convection heat transfer in parallel plate channels with streamwise-periodic rod disturbances. International Journal for Numerical Methods in Fluids, 1998, 28(9): 1371-1387

DOI

12
Yu B, Nie J H, Wang Q W, Tao W Q. Experimental study on the pressure drop and heat transfer characteristics of tubes with internal wave-like longitudinal fins. Heat and Mass Transfer, 1999, 35(1): 65-73

DOI

13
Cheng Y P, Qu Z G, Tao W Q, He Y L. Numerical design of efficient slotted fin surface based on the field synergy principle. Numerical Heat Transfer, Part A, 2004, 45(6): 517-538

DOI

14
Shah R K, Afimiwala K A, Mayne R W. Heat exchanger optimization. In: 6th International Heat Transfer Conference. Washington, DC: Hemisphere Publishing Corp, 1978, 4: 185-191

15
Qu Z G, Tao W Q, He Y L. Three dimensional numerical simulation on laminar heat transfer and fluid flow characteristics of strip fin surface with X-array arrangement of strips. ASME Journal of Heat Transfer, 2004, 126(5): 697-707

DOI

16
Sano Y, Usui H. Evaluation of heat transfer promoters by the fluid dissipation energy. Texas: Scripta Publishing Co., 1982, 91-96

17
Bejan A. General criterion for rating heat exchanger performance. International Journal of Heat and Mass transfer, 1978, 21(5): 655-658

DOI

18
Bejan A. Second law analysis in heat transfer. Energy, 1980, 5(8,9): 721-732

19
William R O, Bejan A. Conservation of available work (exergy) by using promoters of swirl flow in forced convection heat transfer. Energy, 1980, 5(7): 587-596

DOI

20
Chen B H, Huang W H, Second-law analysis for heat transfer enhancement on a rib-type turbulence promoter. Energy, 1988, 13(2): 167-175

DOI

21
Chen B H, Huang W H. Performance evaluation criteria for enhanced heat transfer surface. Int Comm Heat Mass transfer, 1988, 15(1): 59-72

DOI

22
Zimparov V D, Vulchanov N L. Performance evaluation criteria for enhanced heat transfer surfaces. International Communications in Heat and Mass Transfer, 1994, 37(12): 1807-1816

DOI

23
Prasad R C, Shen J H. Performance evaluation of convective heat transfer enhancement devices using exergy analysis. International Journal of Heat and Mass Transfer, 1993, 36(17): 4193-4197

DOI

24
Prasad R C, Shen J H, Performance evaluation using exergy analysis-application to wire-coil inserts in forced convection heat transfer. International Journal of Heat and Mass Transfer, 1994, 37(15): 2297-2303

DOI

25
Guo Z Y, Zhu H Y, Liang X G. Entransy--A physical quantity describing heat transfer ability. International Journal of Heat and Mass Transfer, 2007, 50(13,14): 2545-2556

26
Manglik R M. Heat Transfer Enhancement. In: Bejan A, Kraus A, eds. Heat Transfer Handbook. Hobokin, New Jersey: John Wiley & Son, 2003

27
Fan J F, Ding W K, Zhang J F, He Y L, Tao W Q. A performance evaluation plot of enhanced heat transfer techniques oriented for energy-saving. International Journal of Heat and Mass Transfer, 2009, 52(1, 2): 33-44

28
Yun J Y, Lee K S. Influence of design parameters on the heat transfer and flow friction characteristics of the heat exchanger with slit fins. International Journal of Heat and Mass Transfer, 2000, 43(14): 2529-2539

DOI

29
Bilen K, Yapici S, Celik C. A Taguchi approach for investigation of heat transfer from a surface equipped with rectangular blocks. Energy Conversion and Management, 2001, 42(8): 951-961

DOI

30
Yakut K, Alemdaroglu N, Sahin B, Celik C. Optimum design-parameters of a heat exchanger having exchanger having hexagonal fins. Applied Energy, 2006, 83(2): 82-98

DOI

31
Sanders P A, Thole K A. Effects of winglets to augment tube wall heat transfer in louvered fin heat exchangers. International Journal of Heat and Mass Transfer, 2006, 49(21,22): 4058-4069

32
Fan J F, He Y L, Tao W Q. The flow and heat transfer characteristics of an air side louvered fin-and-tube heat transfer surface with tubes of 4 mm. In: 2nd Asian Symposium on Computational Heat Transfer and Fluid Flow, Jeju, Korea, 2009

33
Tao W Q, Cheng Y P, Lee T S. The Influence of strip location on the pressure drop and heat transfer performance of a slotted fin. Numerical Heat Transfer, Part A: Applications, 2007, 52(5): 463-480

DOI

34
Li Y Y, Xu C R. Experimental Design and Data Processing. Beijing: Chemical Industry Press, 2005

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