lecture6 boundary layers - LTH · 2008-09-17 · von Karman momentum integral equation. 3 ......
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Transcript of lecture6 boundary layers - LTH · 2008-09-17 · von Karman momentum integral equation. 3 ......
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Boundary Layers
Hydromechanics VVR090
Boundar Layer on a Flat Plate
Boundary layer: the zone in which the velocity profile is governed by frictional action
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Boundary layer characterized by a Reynolds number:
3900 laminar flow3900 turbulent flow
δ
δ
δ
δ=
ν
<>
oVR
RR
Viscous sublayer exist close to the surface.
Mathematical implications of boundary layer:
, ,
0,
∂ ∂ ∂ ∂∂ ∂ ∂ ∂
∂ ∂→ ≈ ≈
∂ ∂
u u v vy x x y
u v
p p dpy x dx
von Karman momentum integral equation
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Von Karman momentum integral equation
Apply momentum equation for control volume ABCD.
Height of control volume extends beyond the edge of the boundary layer (to the outer flow).
At edge of the boundary layer: po(x), Vo(x) (known).
Small curvature along body.
Conservation of mass:
[ ]0
0=
⎛ ⎞ρ + ρ =⎜ ⎟
⎝ ⎠∫h
y h
d udy vdx
Conservation of momentum:
[ ] [ ]2
0= =
⎛ ⎞− − τ + τ = ρ + ρ⎜ ⎟
⎝ ⎠∫h
oo y h y h
dp dh u dy uvdx dx
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Develop conservation of mass equation:
0
⎛ ⎞ρ = − ρ⎜ ⎟
⎝ ⎠∫h
o odv udydx
Develop conservation of momentum equation:
2
0
⎛ ⎞− − τ = ρ +ρ⎜ ⎟
⎝ ⎠∫h
oo o o o
dp dh u dy V vdx dx
Combine conservation of mass and momentum:
2
0 0
⎛ ⎞ ⎛ ⎞− − τ = ρ − ρ⎜ ⎟ ⎜ ⎟
⎝ ⎠ ⎝ ⎠∫ ∫h h
oo o
dp d dh u dy V udydx dx dx
Euler eqution for the outer flow:
0=+ρ
= −ρ
oo o
o
o oo o
dp V dV
dp dVVdx dx
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2
0 0
⎛ ⎞ ⎛ ⎞−τ = ρ − ρ −ρ⎜ ⎟ ⎜ ⎟
⎝ ⎠ ⎝ ⎠∫ ∫h h
oo o o o
dVd du dy V udy V hdx dx dx
Combining:
Define displacement thickness:
( )10
ρ δ = ρ −ρ∫h
o o o oV V u dy
Flow rate with and without boundary layer
0
ρ < ρ δ∫h
o oudy V
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1⎛ ⎞ρ
δ = −⎜ ⎟ρ⎝ ⎠∫h
o o
u dyV
In the same manner, define momentum thickness:
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1⎛ ⎞ρ
δ = −⎜ ⎟ρ ⎝ ⎠∫h
o o o
u u dyV V
Substitute in d1 and d2 in momentum equation and express τo in terms of a local friction coefficient cf:
2
2δ
=fc ddx
(constant density, no pressure gradients)
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Laminar Boundary Layer along a Flat Plate
Assume parabolic velocity profile:
( )2
2
2δ −=
δoV y y
u
2
2
2
215
22 15
2215
fo
o
oo o
c dV dx
VdVdx
δ = δ
τ δ= =
ρ
δτ = ρ = μ
δ
2
2
2215
152
30
oo
o
x
VdVdx
xV
x R
δρ = μ
δ
δ μ=ρ
δ=
Integrate the equation:
2 82 15
oo
x
VR
ρτ =
Substitute in dd/dx in shear stress expression:
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Local friction coefficient:
815f
x
cR
≈
Mean friction coefficient along the plate:
0
1 3215
x
f fx
C c dxx R
= =∫
Relationship between Rx and Rd:
2
30xRR δ=
Rd = 3900 Rx = 500,000
(transition between laminar and turbulent conditions in the boundary layer)
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Drag Coefficient for Smooth, Flat Plates
212f f oD C V A= ρ
A: surface area of plate