Analysis of heat transfer and fluid flow thermodynamic irreversibilities is realized on an example of a counter flow double pipe heat exchanger utilizing turbulent air flow as a working fluid. During the process of mathematical model creation and for different working and constructing limitations, total thermodynamic irreversibility is studied. The present work proves that the irreversibility occurred due to unequal capacity flow rates (flow imbalance irreversibility). It is concluded that the heat exchanger should be operated at effectiveness, ε, greater than 0.5 and the well operating conditions will be achieved when ε approaches one where low irreversibility is expected. A new equation is adopted to express the entropy generation numbers for imbalanced heat exchangers of similar design with smallest deviation from the exact value. The results obtained from the new equation are compared with the exact values and with those obtained by Bejan (Bejan, A., 1997, Advanced Engineering Thermodynamics, Wiley, New York).

1.
Bejan
,
A.
, 1977, “
The Concept of Irreversibility in Heat Exchanger Design: Counter Flow Heat Exchangers for Gas-to-Gas Applications
,”
ASME J. Heat Transfer
0022-1481,
99
, pp.
374
380
.
2.
Bejan
,
A.
, 1982,
Entropy Generation Through Heat and Flow
,
Wiley
, New York.
3.
Bejan
,
A.
, 1996, “
Entropy Generation Minimization: The New Thermodynamics of Finite-Size Devices and Finite-Time Processes
,”
J. Appl. Phys.
0021-8979,
79
, pp.
1191
1218
.
4.
Bejan
,
A.
, 1997,
Advanced Engineering Thermodynamics
,
Wiley
, New York.
5.
Aceves-Saborio
,
S.
,
Ranasinghe
,
J.
, and
Reistad
,
G. M.
, 1989, “
An Extension to the Irreversibility Minimization Analysis Applied to Heat Exchangers
,”
ASME J. Heat Transfer
0022-1481,
111
, pp.
29
36
.
6.
Tondeur
,
D.
, and
Kvaalen
,
E.
, 1987, “
Equipartition of Entropy Production. An Optimality Criterion for Transfer and Separation Processes
,”
Ind. Eng. Chem. Res.
0888-5885,
26
, pp.
50
56
.
7.
De Oliveira
,
S.
,
Schwarzer
,
B.
,
Le Goff
,
P.
, and
Tondeur
,
D.
, 1994, “
Optimum Entropy, Exergy and Economics of a Heat Exchanger
,”
Int. Chem. Eng.
0020-6318,
34
(
3
), pp.
351
352
.
8.
Lozano
,
M. A.
, and
Valero
,
A.
, 1993, “
Theory of the Exergetic Costs
,”
Energy
0360-5442,
18
(
9
), pp.
939
960
.
9.
Incorpera
,
F. P.
, and
Dewitt
,
D. P.
, 1996,
Introduction to Heat Transfer
, 3rd ed.,
Wiley
, New York.
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