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
(ʻ
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
).
Search WWH ::
Custom Search