This paper further explores the topic of an ideal heat exchanger, which is still an open question. It is shown that the minimization of entropy production or exergy destruction should not be an objective in heat exchanger design. It is further proven that heat exchanger effectiveness does not correlate with irreversibility. A new performance measure, entropy flux, is introduced and a general expression for its evaluation is presented. It is shown that entropy flux captures many desirable attributes of heat exchangers. For a given effectiveness, a single stream heat exchanger has the absolute maximum entropy flux, and for capacity ratios greater than zero, counterflow has the highest entropy flux, parallel flow the lowest, and the shell and tube heat exchangers are somewhere in between.

1.
Shah
,
R. K.
, and
T.
Skiepko
, 2004, “
Entropy Generation Extrema and Their Relationship With Heat Exchanger Effectiveness—Number of Transfer Unit Behavior for Complex Flow Arrangements
,”
ASME J. Heat Transfer
0022-1481,
126
(
6
), pp.
994
1002
.
2.
Fakheri
,
A.
, 2003, “
The Shell and Tube Heat Exchanger Efficiency and Its Relation to Effectiveness
,”
Proceedings of the 2003 American Society of Mechanical Engineers (ASME) International Mechanical Engineering Congress and Exposition (IMECE)
, Washington, DC, Nov. 16–21.
3.
Fakheri
,
A.
, 2008, “
Efficiency and Effectiveness of Heat Exchanger Series
,”
ASME J. Heat Transfer
0022-1481,
130
(
8
), p.
084502
.
4.
Fakheri
,
A.
, 2007, “
Heat Exchanger Efficiency
,”
ASME J. Heat Transfer
0022-1481,
129
(
9
), pp.
1268
1276
.
5.
Fakheri
,
A.
, 2006, “
Thermal Efficiency of the Cross Flow Heat Exchangers
,”
Proceedings of the 2006 ASME International Mechanical Engineering Conference and Exposition
, Chicago, IL, Nov. 5–10.
6.
McClintock
,
F. A.
, 1951, “
The Design of Heat Exchangers for Minimum Irreversibility
,”
ASME
Paper No. 51-A-108.
7.
Bejan
,
A.
, 1977, “
Concept of Irreversibility in Heat Exchanger Design: Counterflow Heat Exchangers for Gas-to-Gas Applications
,”
ASME J. Heat Transfer
0022-1481,
99
(
3
), pp.
374
380
.
8.
Aceves-Saborio
,
S.
,
Ranasinghe
,
J.
, and
Reistad
,
G. M.
, 1989, “
Extension to the Irreversibility Minimization Analysis Applied to Heat Exchangers
,”
ASME J. Heat Transfer
0022-1481,
111
(
1
), pp.
29
36
.
9.
Badescu
,
V.
, 2004, “
Optimal Strategies for Steady State Heat Exchanger Operation
,”
J. Phys. D
0022-3727,
37
, pp.
2298
2304
.
10.
Johannessen
,
E.
,
Nummedal
,
L.
, and
Kjelstrup
,
S.
, 2002, “
Minimizing the Entropy Production in Heat Exchange
,”
Int. J. Heat Mass Transfer
0017-9310,
45
, pp.
2649
2654
.
11.
Guo
,
J.
,
Cheng
,
L.
, and
Xu
,
M.
, 2010, “
Multi-Objective Optimization of Heat Exchanger Design by Entropy Generation Minimization
,”
ASME J. Heat Transfer
0022-1481,
132
, p.
081801
.
12.
Naterer
,
G. F.
, and
Camberos
,
J. A.
, 2008,
Entropy-Based Design and Analysis of Fluid Engineering Systems
,
CRC Press
,
Boca Raton, FL
.
13.
Bejan
,
A.
, 1996,
Entropy Generation Minimization. The Method of Thermodynamic Optimization of Finite-size Systems and Finite-Time Processes
,
CRC Press
,
New York
.
14.
Shah
,
R. K.
, and
T.
Skiepko
, 2005, “
Exchanger Performance Behavior Through Irreversibility Analysis for 1–2 TEMA G Heat Exchangers
,”
ASME J. Heat Transfer
0022-1481,
127
, pp.
1296
1304
.
15.
Mohamed
,
H. A.
, 2006, “
Entropy Generation in Counter Flow Heat Exchangers
,”
ASME J. Heat Transfer
0022-1481,
128
, pp.
87
92
.
16.
Ogiso
,
K.
, 2003, “
Duality of Heat Exchanger Performance in Balanced Counter-Flow Systems
,”
ASME J. Heat Transfer
0022-1481,
125
, pp.
530
532
.
You do not currently have access to this content.