Abstract

The analogy between heat and mass transfer has been used to obtain local and average heat transfer characteristics over a complete flat tube-fin element with four vortex generators (VGs) per tube. Several types of surfaces involved in heat transfer process such as fin surface mounted with VGs, its back surface (mounted without VGs) and flat tube surface are considered. The mass transfer experiments are performed using naphthalene sublimation method. The effects of the fin spacing and VG parameters such as height and attack angle on heat transfer and pressure drop are investigated. The comparisons of heat transfer enhancement with flat tube-fin element without VG enhancement under three constraints are carried out. The local Nusselt number distribution reveals that VGs can efficiently enhance the heat transfer in the region near flat tube on fin surface mounted with VGs. On its back surface the enhancement is almost the same as on the fin surface mounted with VGs but enhanced region is away from flat tube wall with some distance. Average results reveal that increasing of VG height and attack angle increases the enhancement of heat transfer and pressure drop, whereas small fin spacing causes greater increase of pressure drop. The heat transfer performance, correlations of Nusselt number and friction factor are also given.

1.
Atkinson
,
K. N.
,
Drakulic
,
R.
,
Heikal
,
M. R.
, and
Cowell
,
T. A.
,
1998
, “
Two and Three-Dimensional Numerical Models of Flow and Heat Transfer Over Louvred Fin Arrays in Compact Heat Exchangers
,”
Int. J. Heat Mass Transf.
,
41
, pp.
4063
4080
.
2.
Wang
,
L. B.
,
Jiang
,
G. D.
,
Tao
,
W. Q.
, and
Ozoe
,
H.
,
1998
, “
Numerical Simulation on Heat Transfer and Fluid Flow Characteristics of Arrays With Non-Uniform Plate Length Positioned Obliquely to the Flow Direction
,”
ASME J. Heat Transfer
,
120
, pp.
991
998
.
3.
Wang
,
L. B.
, and
Tao
,
W. Q.
,
1995
, “
Heat Transfer and Fluid Flow Characteristics of Plate-Array Aligned at Angles to the Flow Direction
,”
Int. J. Heat Mass Transf.
,
38
, No.
16
, pp.
3053
3063
.
4.
Fiebig
,
M.
,
1995
, “
Vortex Generators for Compact Heat Exchangers
,”
J. of Enhanced Heat Transfer
,
2
, Nos.
1-2
, pp.
43
61
.
5.
Fiebig
,
M.
,
1995
, “
Embedded Vortices in Internal Flow: Heat Transfer and Pressure Loss Enhancement
,”
Int. J. Heat Mass Transf.
,
16
, pp.
376
388
.
6.
Fiebig
,
M.
,
Valencia
,
A.
, and
Mitra
,
N. K.
,
1994
, “
Local Heat Transfer and Flow Losses in Fin-Tube Heat Exchanger With Vortex Generators: A Comparison of Round and Flat Tubes
,”
Exp. Therm. Fluid Sci.
,
8
, pp.
35
45
.
7.
Fiebig, M., Valencia, A., and Mitra, N. K., 1993, “Wing Type Vortex Generators for Fin-Tube Heat Exchangers,” Proc. 1st International Conference on Aerospace Heat Exchanger Technology, Palo Alto, CA, pp. 467–485.
8.
Goldstein, R. J., 1993, “A Review of Mass (Heat) Transfer Measurements Using Naphthalene Sublimation,” in Experimental Heat Transfer, Fluid Mechanics, and Thermodynamics, Elsevier Science Publishers, B. v. pp. 21–40.
9.
Kylikof, U. A., 1988, The Cooling System of Diesel Locomotive, Moscow (in Russian).
10.
Moffart
,
R. J.
,
1982
, “
Contribution to the Theory of Single-Sample Uncertainty Analysis
,”
ASME J. Heat Transfer
,
104
, pp.
250
260
.
11.
Rich
,
D. G.
,
1973
, “
The Effect of Fin Spacing on Heat Transfer and Friction Performance of Multi-Row, Smooth Plate Fin and Tube Heat Exchanger
,”
ASHRAE Trans.
,
79
, No.
2
, pp.
137
145
.
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