Environmental Engineering Reference
In-Depth Information
where
x
=
cos
θ
,
−
1
≤
x
≤
1. Note that
x
2
d
n
−
1
1
n
d
x
1
n
1
2
1
−
1
d
x
n
−
1
x
2
x
d
n
−
1
d
x
n
−
1
x
2
1
2
n
n
!
x
2
P
n
(
x
)
d
x
=
−
1
−
−
−
1
1
−
x
1
n
d
x
1
n
1
1
d
x
n
−
2
x
2
d
x
n
−
2
x
2
d
n
−
2
d
n
−
2
2
2
n
n
!
=
−
−
1
−
−
−
1
−
1
n
d
x
n
−
3
x
2
d
n
−
3
2
2
n
n
!
1
−
1
=
=
−
0
,
when
n
≥
3
.
Thus we obtain
⎧
⎨
1
3
,
n
=
0
,
1
2
n
+
1
x
2
P
n
(
2
3
C
n
=
x
)
d
x
=
,
n
=
2
,
⎩
2
−
1
0
,
n
=
0
,
2
.
Finally, we have
r
2
cos
2
1
3
+
2
3
r
2
P
2
(
1
3
+
1
3
u
(
r
,
θ
)=
x
)=
θ
−
.
Example 4.
Consider steady heat conduction in a sphere of radius
R
. The tempera-
ture is kept at a constant
v
0
on the upper half of the spherical boundary surface and
at zero on the lower half. Find the steady temperature distribution in the sphere.
Solution
. By the given conditions, the temperature
T
cannot depend on
ϕ
in a spher-
ical coordinate system
(
r
,
θ
,
ϕ
)
. It must satisfy
r
2
∂
sin
⎧
⎨
r
2
∂
1
T
∂
1
r
2
sin
∂
∂θ
θ
∂
T
∂θ
+
=
0
,
∂
r
r
θ
<
<
,
<
θ
<
π
,
0
r
R
0
(7.61)
⎧
⎨
⎩
≤
θ
<
2
,
,
v
0
0
T
(
R
,
θ
)=
2
0
,
<
θ
≤
π
.
⎩
By following a similar approach as that in Example 3, we can obtain the solution of
the Laplace equation in PDS (7.61)
∞
n
=
0
C
n
r
n
P
n
(
cos θ
)
,
where the
C
n
are constants. Applying the boundary condition at
r
T
(
r
,
θ
)=
=
R
yields
v
0
∞
n
=
0
C
n
R
n
P
n
(
x
)=
,
0
<
x
≤
1
,
,−
≤
<
,
0
1
x
0
Search WWH ::
Custom Search