A parametric study has been performed on turbulent flow and heat transfer in internally finned tubes. For a rectangular fin profile, the effects of fin number N, fin width s, fin height H, and helix angle γ were numerically investigated for the conditions of N=1040,H=0.030.1,s=0.050.22,γ=10deg40deg, and Re=40,000. In addition, the performance of three fin profiles—rectangle, triangle, and round crest—with the same fin heights, width, and helix angles were compared for Reynolds numbers between 10,000 and 70,000. Rectangular and triangular fins behave similarly; for some geometric conditions the round crest fin has lower friction factors and Nusselt numbers (17 and 10 percent, respectively) than the rectangular fin. However, when the number of fins is large, the round crest fin can have larger friction factors (about 16 percent). Damping of turbulence energy in the interfin region is credited for the reversal of the typical trends.

1.
Shome
,
B.
, and
Jensen
,
M. K.
,
1996
, “
Experimental Investigation of Variable Property/Mixed Convection Laminar Flow in Internally-Finned Tubes
,”
Journal of Enhanced Heat Transfer
,
4
, pp.
53
70
.
2.
Shome
,
B.
, and
Jensen
,
M. K.
,
1996
, “
Numerical Investigation of Variable Property/Mixed Convection Laminar Flow in Internally-Finned Tubes
,”
Journal of Enhanced Heat Transfer
,
4
, pp.
35
51
.
3.
Bergles, A. E., Jensen, M. K., and Shome, B., 1995, “Bibliography on Enhancement of Convective Heat and Mass Transfer,” Heat Transfer Lab. Report-23, Rensselaer Polytechnic Institute, Troy, New York.
4.
Liu, X., 1998, “Investigation of Turbulent Flow and Heat Transfer in Internally Finned Tubes,” Ph.D. thesis, Rensselaer Polytechnic Institute, Troy, New York.
5.
Carnavos
,
T. C.
,
1979
, “
Cooling Air in Turbulent Flow with Internally Finned Tubes
,”
Heat Transfer Eng.
,
1
, No.
2
, pp.
41
46
.
6.
Carnavos
,
T. C.
,
1980
, “
Heat Transfer Performance of Internally Finned Tubes in Turbulent Flow
,”
Heat Transfer Eng.
,
1
, No.
4
, pp.
32
37
.
7.
Jensen
,
M. K.
, and
Vlakancic
,
A.
,
1999
, “
Experimental Investigation of Turbulent Heat Transfer and Fluid Flow in Internally Finned Tubes
,”
Int. J. Heat Mass Transf.
,
42
, pp.
1343
1351
.
8.
Liu
,
X.
, and
Jensen
,
M. K.
,
1999
, “
Numerical Investigation of Turbulent Flow and Heat Transfer in Internally Finned Tubes
,”
Journal of Enhanced Heat Transfer
,
6
, pp.
105
119
.
9.
Trupp, A. C., Lau, A. C. Y., Said, M. N. A., and Soliman, H. M., 1981, “Turbulent Flow Characteristics in an Internally Finned Tube,” Advances in Heat Transfer-1981, ASME, HTD-18, pp. 11–19.
10.
Edwards
,
D. P.
,
Hirsa
,
A.
, and
Jensen
,
M. K.
,
1996
, “
Turbulent Air Flow in Longitudinally Finned Tubes
,”
ASME J. Fluids Eng.
,
118
, pp.
506
513
.
11.
Patankar
,
S. V.
,
Ivanovic
,
M.
, and
Sparrow
,
E. M.
,
1979
, “
Analysis of Turbulent Flow and Heat Transfer in Internally Finned Tubes and Annuli
,”
ASME J. Heat Transfer
, ,
101
, pp.
29
37
.
12.
Said
,
M. N. A.
, and
Trupp
,
A. C.
,
1984
, “
Predictions of Turbulent Flow and Heat Transfer in Internally Finned Tubes
,”
Chem. Eng. Commun.
,
31
, pp.
65
99
.
13.
Edwards, D. P., and Jensen, M. K., 1994, “An Investigation of Turbulent Flow and Heat Transfer in Longitudinally Finned Tubes,” Heat Transfer Lab. Report HTL-18, Rensselaer Polytechnic Institute, Troy, New York.
14.
Kelkar
,
K. M.
,
1997
, “
Numerical Method for The Computation of Flow in Irregular Domains That Exhibit Geometric Periodicity Using Nonstaggered Grids
,”
Numer. Heat Transfer, Part B
,
31
, pp.
1
21
.
15.
Kern, D. Q., and Kraus, A. D., 1972, Extended Surface Heat Transfer, McGraw-Hill Book Company, New York.
16.
Patankar
,
S. V.
,
Liu
,
C. H.
, and
Sparrow
,
E. M.
,
1977
, “
Fully Developed Flow and Heat Transfer in Ducts Having Streamwise-Periodic Variations of Cross-Sectional Area
,”
ASME J. Heat Trasfer
, ,
99
, pp.
180
186
.
17.
Norris, L. H., and Reynolds, W. C., 1975, “Turbulent Channel Flow With a Moving Wavy Boundary,” Report. FM-10, Department of Mechanical Engineering, Stanford University, CA.
18.
STAR-CD Manuals, 1998, Computational Dynamics, Co., London, U.K.
19.
Vlakancic, A., 1996, “Experimental Investigation of Internally Finned Tube Geometries on Turbulent Heat Transfer and Fluid Flow,” M.S. thesis, Rensselaer Polytechnic Institute, Troy, New York.
20.
Gnielinski
,
V.
,
1976
, “
New Equations for Heat and Mass Transfer in Turbulent Pipe and Channel Flow
,”
Int. Chem. Eng.
,
16
, pp.
359
368
.
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