Environmental Engineering Reference
In-Depth Information
C k ʱ
T
ˆ
S
ʱ ˁ ʱ
c k ʱ
t +
c k ʱ
C k ʱ ʱ ˁ
v
+
J
ʱ ) ·∇
T
+
C k ʱ (
I k ʱ −∇·
d k ʱ )
T
=−∇· p k ʱ v ʱ +
T ʵ˃ SB T 4
H k ʱ d k ʱ ˆ
k T , k ʱ
+
Q k ʱ ,
(90)
where we have used the definitions
U k ʱ =
,
C k ʱ T
(91)
p k ʱ
ˁ k ʱ ,
H k ʱ =
U k ʱ +
(92)
for the specific internal energy and enthalpy of constituent ( k ,
ʱ
). Summing up over
all species, making use of the definitions
n
U ʱ =
c k ʱ U k ʱ ,
(93)
k
=
1
n
C
ʱ =
c k ʱ
C k ʱ ,
(94)
k
=
1
n
p ʱ =
p k ʱ ,
(95)
k
=
1
for the specific internal energy, heat capacity, and pressure of phase
, together with
relation ( 34 ) for the correction factor for energy advection, and then summing up
over all phases, we obtain the temperature equation for the compositional flow
ʱ
C
T
ˆˁ
t +
ʳ C ˁ
C v
+
C ʱ J ʱ
·∇
T
ʱ
T
n
=−∇·
p ʱ v ʱ
H k ʱ D k ʱ ·∇
c k ʱ ˆ
k T
ʱ
ʱ
k
=
1
n
ʵ˃ SB T 4
T
C k ʱ
[ I k ʱ +∇· (
D k ʱ )
]
+
Q
.
(96)
ʱ
k
=
1
Using relations ( 70 ) and ( 71 ) into Eq. ( 96 ) we recover the form of the temperature
equation for the composite system (i.e., the solid and the fluid phases). For a reactive
solid phase, a term of the form
n
T
C kR I kR
(97)
k
=
1
must be added on the right-hand side of Eq. ( 96 ).
 
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