Modeling a fin-and-tube heat exchanger as porous media based on volume averaging theory (VAT), specific geometry can be accounted for in such a way that the details of the original structure can be replaced by their averaged counterparts, and the VAT based governing equations can be solved for a wide range of heat exchanger designs. To complete the VAT based model, proper closure is needed, which is related to a local friction factor and a heat transfer coefficient of a representative elementary volume. The present paper describes an effort to model a fin-and-tube heat exchanger based on VAT and obtain closure for the model. Experiment data and correlations for the air side characteristics of fin-and-tube heat exchangers from the published literature were collected and rescaled using the “porous media” length scale suggested by VAT. The results were surprisingly good, collapsing all the data onto a single curve for friction factor and Nusselt number, respectively. It was shown that using the porous media length scale is very beneficial in collapsing complex data yielding simple heat transfer and friction factor correlations and that by proper scaling, closure is a function of the porous media, which further generalizes macroscale porous media equations. The current work is a step closer to our final goal, which is to develop a universal fast running computational tool for multiple-parameter optimization of heat exchangers.

References

1.
Whitaker
,
S.
, 1972, “
Forced Convection Heat Transfer Correlations for Flow in Pipes, Past Flat Plates, Single Cylinders, Single Spheres, and for Flow in Packed Beds and Tube Bundles
,”
AIChE J.
,
18
(
2
), pp.
361
371
.
2.
Travkin
,
V. S.
, and
Catton
,
I.
, 1995, “
A Two-Temperature Model for Turbulent Flow and Heat Transfer in a Porous Layer
,”
ASME J. Fluids Eng.
,
117
(
1
), pp.
181
188
.
3.
Travkin
,
V. S.
, and
Catton
,
I.
, 1998, “
Porous Media Transport Descriptions—Non-Local, Linear and Non-Linear Against Effective Thermal/Fluid Properties
,”
Adv. Colloid Interface Sci.
,
76-77
, pp.
389
443
.
4.
Rich
,
D. G.
, 1975, “
The Effect of the Number of Tubes Rows on Heat Transfer Performance of Smooth Plate Fin-and-Tube Heat Exchangers
,”
ASHRAE Trans.
,
81
, pp.
307
317
.
5.
McQuiston
,
F. C.
, 1978, “
Correlations of Heat Mass and Momentum Transport Coefficients for Plate-Fin-Tube Heat Transfer Surfaces With Staggered Tubes
,”
ASHRAE Trans., Part
1
(
84
), pp.
294
308
.
6.
Rich
,
D. G.
, 1973, “
The Effect of Fin Spacing on the Heat Transfer and Friction Performance of Multirow, Smooth Plate Fin-and-Tube Heat Exchangers
,”
ASHRAE Trans.
,
79
(
2
), pp.
135
145
.
7.
Gray
,
D. L.
, and
Webb
,
R. L.
, “
Heat Transfer and Friction Correlations for Plate Fin-and-Tube Heat Exchangers Having Plain Fins
,”
Proceedings of the Eighth International Heat Transfer Conference
, pp.
2745
2750
.
8.
Kang
,
H. J.
,
Li
,
W.
,
Li
,
H. Z.
,
Xin
,
R. C.
, and
Tao
,
W. Q.
, 1994, “
Experimental Study on Heat Transfer and Pressure Drop Characteristics of Four Types of Plate Fin-and-Tube Heat Exchanger Surfaces
,”
J. Therm. Sci.
,
3
(
1
), pp.
34
42
.
9.
Wang
,
C.-C.
,
Chi
,
K.-Y.
, and
Chang
,
C.-J.
, 2000, “
Heat Transfer and Friction Characteristics of Plain Fin-and-Tube Heat Exchangers, Part II: Correlation
,”
Int. J. Heat Mass Transfer
,
43
(
15
), pp.
2693
2700
.
10.
Whitaker
,
S.
, 1999,
The Method of Volume Averaging
,
Kluwer Academic
,
Boston
.
11.
Travkin
,
V. S.
, and
Catton
,
I.
, 2001, “
Transport Phenomena in Heterogeneous Media Based on Volume Averaging Theory
,”
Advances in Heat Transfer
,
G. G.
Hari
and
A. H.
Charles
, ed.,
Elsevier
, pp.
1
144
.
12.
Ergun
,
S.
, 1952, “
Fluid Flow Through Packed Columns
,”
Chem. Eng. Prog.
,
48
(
2
), pp.
89
94
.
13.
Vadnjal
,
A.
, 2009, “
Modeling of a Heat Sink and High Heat Flux Vapor Chamber
,” Ph.D. thesis, University of California Los Angeles, Los Angeles.
14.
SAS Institute, Inc.
, 2008, “
JMP® and 8 StatisticsGraphics Guide
,” Volumes 1 and 2, SAS Institute, Inc., Cary, NC.
15.
Zhou
,
F.
,
Hansen
,
N.
, and
Catton
,
I.
, 2010, “
Determining the Computational Domain Length to Obtain Closure for VAT Based Modeling by 3D Numerical Simulation and Field Synergy Analysis
,” ASME Paper No. IMECE 2010-37561.
16.
Tang
,
L.-H.
,
Min
,
Z.
,
Xie
,
G.-N.
, and
Wang
,
Q.-W.
, 2009, “
Fin Pattern Effects on Air-Side Heat Transfer and Friction Characteristics of Fin-and-Tube Heat Exchangers With Large Number of Large-Diameter Tube Rows
,”
Heat Transfer Eng.
,
30
(
3
), pp.
171
180
.
17.
Tang
,
L. H.
,
Zeng
,
M.
, and
Wang
,
Q. W.
, 2009, “
Experimental and Numerical Investigation on Air-Side Performance of Fin-and-Tube Heat Exchangers With Various Fin Patterns
,”
Exp. Therm. Fluid Sci.
,
33
(
5
), pp.
818
827
.
18.
Xie
,
G.
,
Wang
,
Q.
, and
Sunden
,
B.
, 2009, “
Parametric Study and Multiple Correlations on Air-Side Heat Transfer and Friction Characteristics of Fin-and-Tube Heat Exchangers With Large Number of Large-Diameter Tube Rows
,”
Appl. Therm. Eng.
,
29
(
1
), pp.
1
16
.
19.
Wang
,
C.-C.
, and
Chi
,
K.-Y.
, 2000, “
Heat Transfer and Friction Characteristics of Plain Fin-and-Tube Heat Exchangers, Part I: New Experimental Data
,”
Int. J. Heat Mass Transfer
,
43
(
15
), pp.
2681
2691
.
20.
Tang
,
L. H.
,
Xie
,
G. N.
,
Zeng
,
M.
,
Wang
,
H. G.
,
Yan
,
X. H.
, and
Wang
,
Q. W.
, 2007, “
Experimental Investigation on Heat Transfer and Flow Friction Characteristics in Three Types of Plate Fin-and-Tube Heat Exchangers
,”
J. Xi’an Jiaotong Univ.
,
41
, pp.
521
525
(in Chinese).
21.
Techo
,
R.
,
Tickner
,
R. R.
, and
James
,
R. E.
, 1965, “
An Accurate Equation for the Computation of the Friction Factor for Smooth Pipes for the Reynolds Number
,”
ASME J. Appl. Mech.
,
32
, p.
443
.
You do not currently have access to this content.