Civil Engineering Reference
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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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