While the concept of minimum irreversibility is associated with the maximum energy efficiency for energy conversion processes in thermal systems, we have found that it is not quite applicable to the heat exchanger analysis. We have shown that the heat exchanger effectiveness can be maximum, having an intermediate value or minimum at the maximum irreversibility operating point depending on the flow arrangement of the two fluids. Similarly, the heat exchanger effectiveness can be minimum or maximum at the minimum irreversibility operating point. The objective of this paper is to illustrate and discuss such heat exchanger performance and irreversibility trends by combining the temperature difference irreversibility with the P-NTU results for complex flow arrangements.

1.
Kays, W. M., and London, A. L., 1998, Compact Heat Exchangers, Krieger Publishing, Malabar, FL.
2.
Pignotti
,
A.
, and
Shah
,
R. K.
,
1992
, “
Effectiveness-Number of Transfer Units Relationships for Heat Exchanger Complex Flow Arrangements
,”
Int. J. Heat Mass Transfer
,
35
, pp.
1275
1291
.
3.
Shah, R. K., and Sekulic, D. P., 1998, “Heat Exchangers,” in Handbook of Heat Transfer, W. M. Rohsenow, J. P. Hartnett, and Y. I. Cho, eds., McGraw-Hill, New York, Chap. 17.
4.
Kandlikar
,
S. G.
, and
Shah
,
R. K.
,
1989
, “
Asymptotic Effectiveness-NTU Formulas for Multipass Plate Heat Exchangers
,”
ASME J. Heat Transfer
,
111
, pp.
314
321
.
5.
Sekulic
,
D. P.
,
1990
, “
The Second Law Quality of Energy Transformation in a Heat Exchanger
,”
ASME J. Heat Transfer
,
112
, pp.
295
300
.
6.
Kern D. Q., 1950, Process Heat Transfer, McGraw-Hill, New York.
7.
Shah R. K., 1983, “Heat Exchanger Basic Design Methods,” in Low Reynolds Number Flow Heat Exchangers, S. Kakac¸, R. K. Shah, and A. E. Bergles, eds., Hemisphere Publishing Corp. Washington, DC, pp. 21–72.
8.
Bejan
,
A.
,
1977
, “
The Concept of Irreversibility in Heat Exchanger Design: Counterflow Heat Exchangers for Gas-to-Gas Applications
,”
ASME J. Heat Transfer
,
99
, pp.
374
380
.
9.
Bejan A., 1982, “Second-Law Analysis in Heat Transfer and Thermal Design,” Advances in Heat Transfer, T. F. Irvine and J. P. Hartnett, eds., 15, pp. 1–58.
10.
Sekulic
,
D. P.
,
1986
, “
Entropy Generation in a Heat Exchanger
,”
Heat Transfer Eng.
,
7
(
1-2
), pp.
83
88
.
11.
Hesselgreaves
,
J. E.
,
2000
, “
Rationalization of Second Law Analysis of Heat Exchangers
,”
Int. J. Heat Mass Transfer
,
43
, pp.
4189
4204
.
12.
Kmecko I., 1998, “Paradoxical Irreversibility of Enthalpy Exchange in Some Heat Exchangers,” M.S. thesis, University of Novi Sad, Novi Sad, Yugoslavia.
13.
Witte
,
L. C.
,
1988
, “
The Influence of Availability Costs on Optimal Heat Exchanger Design
,”
ASME J. Heat Transfer
,
110
, pp.
830
835
.
14.
Ogiso K., 2002, “Duality of Heat Exchanger Performance in Balanced Counter-Flow Systems,” Proc. of the International Symposium on Compact Heat Exchangers, G. P. Celata et al., eds., Edizioni ETS, Pisa, pp. 203–205.
15.
London
,
A. L.
,
1982
, “
Economics and the Second Law: An Engineering View and Methodology
,”
Int. J. Heat Mass Transfer
,
25
, pp.
743
751
.
1.
London, A. L., and Shah, R. K., 1983, “Costs of Irreversibilities in Heat Exchanger Design,” Heat Transfer Engineering, 4(2), pp. 59–73;
2.
Discussion by W. Roetzel, in 5(3-4), 1984, pp. 15, 17, and 6(2), 1985, p. 73.
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