Shell and tube heat exchangers (STHXs) have their pioneer use in industrial applications. The scope of this work is to design and optimize shell and tube heat exchanger of five distinct material combinations to comply with the requirements of effectiveness (heat recovery) and total cost as objective functions. For this purpose; thermal design is conducted according to TEMA specification in which tube outer diameter, length of tube, tube pitch, shell diameter, baffle spacing and baffle thickness are considered as primary design parameters. Ɛ-NTU method and Kern method are used to estimate tube side and shell side heat transfer coefficient and pressure drop respectively. For optimization, non-dominated sorting genetic algorithm (NSGA-II) is implemented in Python to attain a set of multiple optimum solutions called ‘Pareto optimal solutions’ stating the maximum effectiveness and the minimum total cost. The range of design parameters of pareto optimal solutions are also reported. Furthermore, responsiveness of total cost with respect to effectiveness of pareto optimal fronts are addressed. The percentage change of effectiveness and total cost are analyzed for 20% increase of input design parameters. Finally, a case study is explored where the optimized design parameters are selected from the pareto optimal fronts depicting the optimal cost about $11400 with effectiveness 0.68. After the different fundamental dimensions are obtained from the thermal design, a detailed mechanical design is also achieved using TEMA specification.

1.
Mirzaei
,
M.
,
Hajabdollahi
,
H.
and
Fadakar
,
H.
,
2017
.
Multi-objective optimization of shell-and-tube heat exchanger by constructal theory
.
Applied Thermal Engineering
,
125
, pp.
9
19
.
2.
Ramananda
RAO
, K.,
Shrinivasa
,
U.
and
Srinivasan
,
J.
,
1991
.
Synthesis of cost-optimal shell-and-tube heat exchangers
.
Heat transfer engineering
,
12
(
3
), pp.
55
477
.
3.
Caputo
,
A.C.
,
Pelagagge
,
P.M.
and
Salini
,
P.
,
2008
.
Heat exchanger design based on economic optimisation
.
Applied thermal engineering
,
28
(
10
), pp.
1151
1159
.
4.
Cao
,
E.
,
2009
.
Heat transfer in process engineering
.
McGraw Hill Professional
.
5.
Standards of the Tubular Exchanger Manufactures Association, nineth ed.,
TEMA
,
Tarrytown, NY
,
2007
.
6.
Taal
,
M.
,
Bulatov
,
I.
,
Klemeš
,
J.
and
Stehlík
,
P.
,
2003
.
Cost estimation and energy price forecasts for economic evaluation of retrofit projects
.
Applied thermal engineering
,
23
(
14
), pp.
1819
1835
.
7.
Srinivas
,
N.
and
Deb
,
K.
,
1994
.
Muiltiobjective optimization using nondominated sorting in genetic algorithms
.
Evolutionary computation
,
2
(
3
), pp.
221
248
.
8.
Deb
,
K.
,
Pratap
,
A.
,
Agarwal
,
S.
and
Meyarivan
,
T.A.M.T.
,
2002
.
A fast and elitist multiobjective genetic algorithm: NSGA-II
.
IEEE transactions on evolutionary computation
,
6
(
2
), pp.
182
197
.
9.
Sanaye
,
S.
and
Hajabdollahi
,
H.
,
2010
.
Multi-objective optimization of shell and tube heat exchangers
.
Applied Thermal Engineering
,
30
(
14-15
), pp.
1937
1945
.
10.
Mukherjee
,
R.
,
2004
.
Practical Thermal Design of Shell and Tube Heat Exchangers
.
11.
Mukherjee
,
R.
,
1998
.
Effectively design shell-and-tube heat exchangers
.
Chemical Engineering Progress
,
94
(
2
), pp.
21
37
.
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