Environmental Engineering Reference
In-Depth Information
)
β
∂
T
β
β
∂
k
β
T
β
d
A
∈
β
∇
T
β
β
1
V
REV
∈
β
(
ρ
c
=
∇
·
+
n
βσ
t
A
βσ
k
β
∇
T
β
β
d
A
1
V
REV
+
n
βσ
·
A
βσ
1
V
REV
T
β
d
A
+
n
βσ
·
k
β
∇
,
(6.269)
A
βσ
and
k
σ
∈
σ
∇
T
σ
d
A
T
σ
σ
∂
)
σ
∂
1
V
REV
T
σ
σ
+
∈
σ
(
ρ
c
=
∇
·
n
σβ
t
A
βσ
1
V
REV
T
σ
σ
d
A
+
n
σβ
·
k
σ
∇
A
βσ
1
V
REV
T
σ
d
A
+
n
σβ
·
.
k
σ
∇
(6.270)
A
βσ
After developing the closure for
T
β
and
T
σ
, Quintard and Whitaker (1993) obtain a
two-equation model
)
β
∂
T
β
β
∂
K
ββ
·
∇
T
β
β
T
σ
σ
∈
β
(
ρ
c
=
∇
·
+
K
βσ
·
∇
t
T
σ
σ
−
T
β
β
+
ha
υ
,
(6.271)
and
K
σσ
·
∇
K
σβ
·
∇
T
β
β
T
σ
σ
∂
)
σ
∂
T
σ
σ
+
∈
σ
(
ρ
c
=
∇
·
t
T
σ
σ
−
T
β
β
−
ha
υ
,
(6.272)
where
h
and
a
υ
come from modeling of the interfacial flux and are the film heat
transfer coefficient and the interfacial area per unit volume, respectively.
K
ββ
,
K
σσ
,
K
βσ
and
K
σβ
are the effective thermal conductivity tensors, and the coupled ther-
mal conductivity tensors are equal
K
βσ
=
K
σβ
.
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