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
2τ
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
2τ
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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