Environmental Engineering Reference
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) 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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