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
 
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