Environmental Engineering Reference
In-Depth Information
Assume
u
=
T
(
t
)
v
(
r
,
θ
,
ϕ
)
. Substituting it into the equation of PDS (6.141) yields,
k
2
as the separation constant,
with
−
λ
=
−
1
T
+
τ
0
T
B
2
T
=
Δ
v
(
r
,
θ
,
ϕ
)
k
2
,
θ
,
ϕ
)
=
−
λ
=
−
.
A
2
T
+
v
(
r
Thus we arrive at
1
τ
0
+
λ
B
2
T
(
T
(
A
2
T
t
)+
t
)+
λ
(
t
)=
0
(6.142)
and
k
2
v
(
,
θ
,
ϕ
)+
(
,
θ
,
ϕ
)=
,
<
<
,
<
θ
<
π
,
Δ
v
r
r
0
0
r
a
0
(6.143)
L
(
v
,
v
r
)
|
r
=
a
=
0
.
The solution of the latter is available in Section 2.6.2
P
n
(
v
mnl
(
r
,
θ
,
ϕ
)=(
a
mnl
cos
m
ϕ
+
b
mnl
sin
m
ϕ
)
cos
θ
)
j
n
(
k
nl
r
)
,
m
≤
n
,
a
2
n
2
1
+
k
nl
=
where constants
a
mnl
and
b
mnl
are not all zero,
λ
=
μ
,
n
=
l
n
+
2
1
0
,
1
,
2
, ···
,
l
=
1
,
2
, ···
and the
μ
are available in Section 2.6.2. Substituting
l
a
2
n
+
2
1
k
nl
=
λ
=
μ
into Eq. (6.142) yields
l
1
τ
0
+(
2
T
nl
(
T
nl
2
T
nl
(
(
t
)+
k
nl
B
)
t
)+(
k
nl
A
)
t
)=
0
.
Its characteristic roots read
1
τ
0
+(
1
τ
0
+(
2
2
2
2
−
k
nl
B
)
±
k
nl
B
)
−
4
(
k
nl
A
)
r
1
,
2
=
(6.144)
2
=
α
nl
±
β
nl
i
.
Thus
e
α
nl
t
T
nl
(
t
)=
(
c
nl
cos
β
nl
t
+
d
nl
sin
β
nl
t
)
.
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