Environmental Engineering Reference
In-Depth Information
Table 4.4
The Nusselt number correlations used in the parallel-plate AMR models
Nusselt number correlation
Note
Conditions of validation
Used in the
AMR
model by
References
1
=
3
:
592
0.1 < Gz <10
6
3
:
592
ð
Þ
d
h
L
RePr
Tu
ek
et al. [
17
],
Nielsen
et al. [
83
]
š
Nickolay
and Martin
[
84
]
Gz
¼
Nu
¼
7
:
541
3
:
592
þ
1
:
841Gz
1
=ðÞ
For fully developed laminar
fl
ow
1
=
3
:
592
3
:
592
d
h
For developing laminar
fl
ow
Petersen
et al. [
82
]
ð
Þ
Gz
ð
x
Þ¼
x
RePr
1
=ðÞ
541
3
:
592
Nu x
ðÞ¼
7
:
þ
1
:
841Gz
ð
x
Þ
Nu
¼
7
:
54
For a fully developed laminar
ow and a
constant heat transfer wall temperature (the
latter is not actually the case in the AMR)
fl
Chiba et al.
[
48
]
Bejan
et al. [
85
]
0
@
1
A
1
2
:
61R
þ
4
:
97R
2
5
:
119R
3
R is the aspect
ratio of the fluid
channel
For fully developed laminar flow
Nikkola
et al. [
47
]
Kandlikar
et al. [
86
]
þ
2
:
702R
4
0
:
548R
5
Nu
¼
7
:
541
!
1
=
2
2
R is the aspect
ratio of the fluid
channel
For developing laminar flow
Risser
et al. [
44
]
Bavie
'
re
et al. [
87
]
1
=
2
x
d
h
Re
1
Pr
2
Nu
¼
0
:
41
þW
0
@
1
A
0853R
2
1
2
:
0421R
þ
3
:
2
:
4765R
3
þ
1
:
0578R
4
0
:
1861R
5
W ¼
8
:
235
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