Environmental Engineering Reference
In-Depth Information
Remark 1. Note that I 0 (
x
)=
I 1 (
x
)
. The solution of PDS (5.15) at f
= ψ =
0 is thus
ϕ x
at τ 0 + ϕ x
at τ 0
1
W ϕ (
+
τ 0 +
t
0
e
u
=
x
,
t
)=
t
2
τ 0
a
1
2
a
τ 0 ξ d
c 2 t
y
1
2
x + t
ξ
+
τ 0 I 0 (
y
)+
I 1 (
y
)
ϕ
,
(5.27)
τ 0
a
x
t
τ 0
a
ξ 2
t 2
where y
=
c
x
. Also, the solution of PDS (5.15) at
ψ = ϕ =
0
reads
t
u
=
W f τ (
x
,
t
τ )
d
τ
0
c
ξ 2
τ 0
a
2
I 0
(
t
τ )
x
τ 0
a
f a
d
t
ξ
τ 0 , τ
x
+
t
1
2
t
τ
0 d
e
ξ .
=
τ
τ a x t
τ 0
0
(5.28)
[ ξ ]=[ τ 0 x
[ ξ ]=
Since
/
a
]=
T ,wehave
T ,
[
y
]=
1and
[
I 0 ]=
1. Therefore,
ξ ]= Θ
T 1
Eq. (5.26):
[
u
]=[
I 0 ][ ψ ][
d
·
T
= Θ
.
c 2 t
y
ξ
T 1
Eq. (5.27):
[
u
]=
I 1 ϕ
d
=
Θ
T
= Θ
(The unit of all the other terms is
also clear.)
d
ξ
I 0
τ 0 f d
T 1
T 1 T
Eq. (5.28):
[
u
]=
τ
=
T
·
· Θ
= Θ
.
Remark 2. Rewrite PDS (5.15) into
u t
τ
f
(
x
,
t
)
A 2 u xx +
0 +
u tt =
, − <
x
< + ,
0
<
t
,
τ
(5.29)
0
u
(
x
,
0
)= ϕ (
x
) ,
u t
(
x 0
)= ψ (
x
) ,
a τ 0 [
LT 1 is the velocity of thermal waves. For a variable
where A
=
A
]=
τ 0
a ξ
ξ =
transformation
,
τ 0
a
1
A d
ξ =
ξ =
ξ ,
d
d
c t 2
b
τ 0
a
ξ 2
2 a τ 0 .
2
2
y
=
x
=
(
At
)
(
x
ξ )
,
b
=
1
/
 
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