Civil Engineering Reference
In-Depth Information
0
0
0
dU
1
∂
P
()
()
[4.50]
∫
∫
∫
2
ds
=−
sds
+ ∇
ν
U sds
dt
ρ∂
x
−
t
−
t
−
t
where
U
and
P
are, respectively, the local instantaneous
velocity and pressure (which include their mean and
fluctuating values). All the quantities are now a function of
the curvilinear coordinate
s
. Equation [4.50] becomes
0
0
1
∂
P
()
( )
() ()
()
()
[4.51]
⎦
∫
∫
2
u
0
=−+
u t
⎡
U
−−
t
U
0
⎤
−
sds
+ ∇
ν
U sds
⎣
ρ∂
x
−
t
−
t
The notation
(
s
)
indicates the quantities evaluated along
the trajectory of the particle at time
t
. By multiplying the
above equation by
v
0
()
and finding the overall mean, we find
0
1
∂
P
()()
()() () () ()
()
()
⎡
⎤
∫
uv
00
=−
ut v
0
+
v Ut
0
−−
U
0
−
v
0
s s
⎣
⎦
ρ
∂
x
−
t
[4.52]
0
()
()
∫
2
+
ν
v
0
∇
Us ds
−
t
Th
e velocity
U
of the fluid particle
is decomposed into
is evaluated at
the point traversed by the fluid particle at time
u
. The mean Eulerian velocity
U
()
U
=
U
+
−
t
t
. It is
−
expressed in a Taylor series by
0
dU
()
()
()
()
[4.53]
∫
Ut
−=
U
0
−
vs
0
s
dy
−
t
of the first order. Equat
io
n
[4
.53] is a direct consequence of
equation [4.42], with
Q
U
. After substituting equation
[4.53] back into equation [4.51] and multiplied the relation
thus obtained by
v
, we find
=
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