introduction to the boundary layer concept
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Introduction to the Boundary Layer concept. Content : Introduction to the Bounday Layer concept; Constraint and unconstraint boundary layers Free shear flows and wakes Laminar and turbulent boundary layers; Boundary layer separation; Thin boundary layer equations - PowerPoint PPT PresentationTRANSCRIPT
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer concept Content:
– Introduction to the Bounday Layer concept;
– Constraint and unconstraint boundary layers
– Free shear flows and wakes
– Laminar and turbulent boundary layers;
– Boundary layer separation;
– Thin boundary layer equations
– Longitudinal pressure gradient effects on the boundary layer growth.
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer
Movies (6), 88, 89
MFM: BL, Impulsive Started Flow, Overview
MFM: BL, BL Concepts,Viscous effects near boundaries
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer Boundary layer: flow region in the vicinity of a wall
where viscous/diffusive effects and energy dissipation are significative.
U U
x
y Outer invisicid flow
Boundary layer: significantyu
(x)
Boundary layer width: u0,99 U
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer Streamlines over a flat plat
1. The streamlines moves away slowly from the wall. Why?
U U
x
y Limit strealine of Boundary layer
Streamlines
2. This separation of streamlines is most intense outside the boundary layer. Why?
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer Notes about boundary layer:
1. The boundary layer may be laminar or turbulent
2. Thin boundary layer if (x)<<x
3. Boundary layer confined: cannot grow free (ex: tube or between plates)
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer Constrained Boundary Layer:
(x) Fully Developed Velocity ProfielEntrance Region
Boundary Layer
External Flow
1. Entrance region: the velocity increases at the center line (to keep the mass flow rate) and the pressure falls (Bernoulli’s Equation)–> dp/dx<0.
2. After the union of all boundary layers, all the flow is boundary layer flow . In turbulent flow, the eddy dimension is limited by d.
Rx
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer Boundary layer in external flows (unconstrained)
1. is not limited, it grows with the distance to the leading edge x (beginning).
2. Nondimensional velocity profile can stabilize
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer
Shear flows (longitudinal convective transport of momentum
affected by diffusion):
o Free Shear Flows: ex: free jet
o Wake: flow zone resulting from the joining of the boundary layers on the two faces of the plate
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer Transition from laminar to turbulent:
Ux
cesviscousfor
rcesinertialfoRe x – Start of Boundary Layer (BL)
•Start of BL: 0x 0Re Laminar Flow
•Long plate: Re increases
Critical Re (5105)
Transition to turbulent
00 yyu Very high
00 yyu decreases
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Introduction to the Boundary Layer Regions of turbulent boundary layer:
– Linear sub-layer or laminar sub-layer;– Transition layer;– Logaritmical profile zone;– Outer zone (turbulent vorticity and non turbulent outer flow).
mfm – BL/ Instability, Transition and Turbulence:Boundary Layer transitionFully turbulent BL flowInstability and transition in pipe and duct flow
Fully turbulent duct flow
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Laminar Thin Boundary Layer Equations (<<x) over flat plate
Steady flow, e constants. Streamlines slightly divergents0 yp
dxdpxp e
2
2
2
21
y
u
x
u
x
p
y
uv
x
uu
2D Navier-Stokes Equations at x direction:
Compared with 2
2
y
u
dxdpe
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Laminar Thin Boundary Layer Equations (<<x) over flat plate
2
21
y
u
dx
dp
y
uv
x
uu e
Laminar thin boundary layer equations (<<x) to flat plates
pe external pressure, can be calculated bu Bernoulli’s Equation because there is not viscous effects outer the Boundary Layer
Note 1. The plate is considered flat if d is lower then the local curvature radius
Note 2. At the separation point, the BD grows a lot and no longer thin
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
z
wu
y
vu
x
uu
y
u
dx
dp
y
uv
x
uu e
2
21
Turbulent Thin Boundary Layer Equations (<<x) over flat plate
2D Thin Turbulent Boundary Layer Equation (<<x) to flat plates:
Resulting from Reynolds Tensions (note the w term)
0 0
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Boundary Layer Separation Boundary Layer Separation: reversal of the flow by
the action of an adverse pressure gradient (pressure increases in flow’s direction) + viscous effects
mfm: BL / Separation / Flow over edges and blunt bodies
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Boundary Layer Separation Boundary layer separation: reversal of the flow by the
action of an adverse pressure gradient (pressure increases in flow’s direction) + viscous effects
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Boundary Layer Separation Bidimensional (2D) Thin Boundary Layer (<<x)
Equations to flat plates:
2
21
y
u
dx
dp
y
uv
x
uu e
Close to the wall (y=0) u=v=0 :
dx
dp
y
u e
y1
0
2
2
Similar results to turbulent boundary layer - close to the wall there is laminar/linear sub-layer region.
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Boundary Layer Separation Outside Boundary layer: 0
2
2
y
u
The external pressure gradient can be:o dpe/dx=0 <–> U0 constant (Paralell outer streamlines):
o dpe/dx>0 <–> U0 decreases (Divergent outer streamlines):
o dpe/dx<0 <–> U0 increases (Convergent outer streamlines):
Close to the wall (y=0) u=v=0 :
dx
dp
y
u e
y1
0
2
2
Same sign
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Zero pressure gradient:dpe/dx=0 <–> U0 constant (Paralell outer streamlines):
y
u
Inflection point at the wall
No separation of boundary layer
02
2
yy
u
00
2
2
yy
u
Boundary Layer Separation
Curvature of velocity profile is constant
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Favourable pressure gradient:dpe/dx<0 <–> U0 increases (Convergent outer streamlines):
02
2
yy
u y
00
2
2
yy
u
Curvature of velocity profile remains constant
No boundary layer separation
Boundary Layer Separation
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Adverse pressure gradient:dpe/dx>0 <–> U0 decreases (Divergent outer streamlines):
02
2
yy
u
00
2
2
yy
u Curvature of velocity profile can change
Boundary layer Separation can occur
y
P.I.
Boundary Layer Separation
Separated Boundary Layer
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Sum of viscous forces:2
2
y
u
Become zero with velocity
Can not cause by itself the fluid stagnation (and the separation of Boundary Layer)
Boundary Layer Separation
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Effect of longitudinal pressure gradient:
0dx
dpe (Convergent outer streamlines)
0dx
dpe (Divergent outer streamlines)
Viscous effects retarded Viscous effects reinforced
Fuller velocity profiles
Less full velocity profiles
...11
dx
dp
ux
u e
Decreases BL growth Increases BL growths
Boundary Layer Separation
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Effect of longitudinal pressure gradient:
Fuller velocity profiles
Less full velocity profiles
...11
dx
dp
ux
u e
Decreases BL growth Increases BL growths
Fuller velocity profiles – more resistant to adverse pressure gradients
Turbulent flows (fuller profiles)- more resistant to adverse pressure gradients
Boundary Layer Separation
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Boundary Layer Sepaation
Longitudinal and intense adverse pressure gradient does not cause separation
=> there’s not viscous forces
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
No viscous forces – no separation of Boundary Layer:
(ds displacement over a streamline)
V=0 (stagnation point) 0ds
dp
ds
dp
ds
dVV
1
Boundary Layer Separation
From pressure forcesNo reversal of the flow
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
MECÂNICA DOS FLUIDOS II Contents:
– Boundary Layer;
– Boundary Layer thickness;
– Limiting line of Boundary Layer;
– Deviation of streamlines at Boundary Layer;
– Thin Boundary Layer;
– Constrained and unconstrained boundary layer;
– Free Shear flows;
– Wakes;
– Thin boundary layer equations.
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
Contents:– Boundary Layer Separation: conditions to separation
– Adverse, favourable and zero pressure gradient;
– Effects of pressure gradient on the Boundary layer evolution
Separação da Camada limite
2004 Mecânica dos Fluidos II Prof. António Sarmento - DEM/IST
MECÂNICA DOS FLUIDOS II
Bibliography :– Sabersky – Fluid Flow: 8.1, 8.2
– White – Fluid Mechanics: 7.1, 7.3, 7.5