The aim of this paper is the analysis of heat transfer in a radial fin assembly during the process of dehumidification. An individual finned tube geometry is a reasonable representation of heat exchangers used in air conditioning. The condensation process involves both heat and mass transfer and the cooling takes place by the removal of sensible as well as latent heat. The ratio of sensible to total heat is an important quantity that defines the heat transfer process during a dehumidifier operation. A one-dimensional model for heat transfer in the fin and the heat exchanger block is developed to study the effects of condensation on the fin surface. The combined heat and mass transfer process is modeled by incorporating the ratio of sensible to total heat in the formulation. The augmentation of heat transfer due to fin was established by comparing the heat transfer rate with and without fins under the same operating conditions. Calculations were carried out to study the effects of relative humidity and dry bulb temperature of the incoming air, and cold fluid temperature inside the coil on the performance of the heat exchanger. An analysis of the overall efficiency for the assembly was also done. Results were compared to those under dry conditions, wherever appropriate. Comparison between present results and those published for rectangular as well as radial fins under fully wet conditions were made. These comparisons established the validity of the present model. It was found that the heat transfer rate increased with increment in both dry bulb temperature and relative humidity of the air. The augmentation factor, however, decreased with increment in relative humidity and the dry bulb temperature. The fin efficiency decreased with relative humidity.

1.
ASHRAE, 1993, Handbook of Fundamentals, Atlanta, GA.
2.
Coney
 
J. E. R.
,
Kazeminejad
 
H.
, and
Sheppard
 
C. G. W.
,
1989
a, “
Dehumidification of Air on a Vertical Rectangular Fin: A Numerical Study
,”
Journal of Mechanical Engineering Science
, Vol.
203
, pp.
165
175
.
3.
Coney
 
J. E. R.
,
Kazeminejad
 
H.
, and
Sheppard
 
C. G. W.
,
1989
b, “
Dehumidification of Turbulent Air Flow over a Thick Fin: An Experimental Study
,”
Journal of Mechanical Engineering Science
, Vol.
203
, pp.
177
188
.
4.
Hong
 
T. K.
, and
Webb
 
R. L.
,
1996
, “
Calculation of Fin Efficiency for Wet and Dry Fins
,”
International Journal of HVAC & R Research
, Vol.
2
, No.
1
, pp.
27
41
.
5.
Kays, W. M., and London, A. L., 1964, Compact Heat Exchangers, McGraw Hill, New York, NY.
6.
Kazeminejad
 
H.
,
1995
, “
Analysis of One-Dimensional Fin Assembly Heat Transfer with Dehumidification
,”
International Journal of Heat and Mass Transfer
, Vol.
38
, No.
3
, pp.
455
462
.
7.
Kazeminejad
 
H.
,
Yaghoubi
 
M. A.
, and
Bahri
 
F.
,
1993
, “
Conjugate Forced Convection-Conduction Analysis of the Performance of a Cooling and Dehumidifying Vertical Rectangular Fin
,”
International Journal of Heat and Mass Transfer
, Vol.
36
, pp.
3625
3631
.
8.
Kern, D. Q., and Kraus, A. D., 1972, Extended Surface Heat Transfer, McGraw Hill, New York, NY.
9.
Kraus, A. D., 1982, Analysis and Evaluation of Extended Surface Thermal Systems, McGraw Hill, New York, NY.
10.
McQuiston
 
F. C.
,
1975
, “
Fin Efficiency with Combined Heat and Mass Transfer
,”
ASHRAE Transactions
, Vol.
81
, Part 1, pp.
350
355
.
11.
McQuiston
 
F. C.
,
1978
, “
Heat, Mass, and Momentum Transfer Data for Five Plate-Fin-Tube Heat Transfer Surfaces
,”
ASHRAE Transactions
, Vol.
84
, Part 1, pp.
266
293
.
12.
McQuiston, F. C., and Parker, J. D., 1994, Heating, Ventilating, and Air Conditioning, 4th Edition, John Wiley & Sons, Inc., New York, NY.
13.
O¨zisik, M. N., 1993, Heat Conduction, 2nd Edition, John Wiley & Sons, New York, NY.
14.
Schmidt
 
T. E.
,
1949
, “
Heat Transfer Calculations for Extended Surfaces
,”
Refrigerating Engineering
, Vol.
49
, pp.
351
357
.
15.
Threlkeld, J. L., 1970, Thermal Environmental Engineering, Prentice-Hall, New York, NY.
16.
Wang
 
C.
,
Hsieh
 
Y.
, and
Lin
 
Y.
,
1997
, “
Performance of Plate Finned Tube Heat Exchangers Under Dehumidifying Conditions
,”
Journal of Heat Transfer
, Vol.
119
, pp.
109
117
.
17.
Webb, R. L., 1994, Principles of Enhanced Heat Transfer, John Wiley & Sons, New York, NY.
18.
Wu
 
G.
, and
Bong
 
T. Y.
,
1994
, “
Overall Efficiency of a Straight Fin with Combined Heat and Mass Transfer
,”
ASHRAE Transactions
, Vol.
100
, Part 1, pp.
367
374
.
This content is only available via PDF.
You do not currently have access to this content.