WALL FREE SHEAR FLOW

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WALL FREE SHEAR FLOW Turbulent flows free of solid boundaries JET Two-dimensional image of an axisymmetric water jet, obtained by the laser-induced fluorescence technique. (From R. R. Prasad and K. R. Sreenivasan, Measurement and interpretation of fractal dimension of the scalar interface in turbulent flows, Phys. Fluids A, 2:792–807, 1990) x y Irrotational Turbulent

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WALL FREE SHEAR FLOW. Turbulent flows free of solid boundaries. Irrotational. JET. y. x. Turbulent. - PowerPoint PPT Presentation

Transcript of WALL FREE SHEAR FLOW

Page 1: WALL FREE SHEAR FLOW

WALL FREE SHEAR FLOWTurbulent flows free of solid boundaries

JET

Two-dimensional image of an axisymmetric water jet, obtained by the laser-induced fluorescence technique. (From R. R. Prasad and K. R. Sreenivasan, Measurement and interpretation of fractal dimension of the scalar interface in turbulent flows, Phys. Fluids A, 2:792–807, 1990)

x

y

Irrotational

Turbulent

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WAKE

http://www.ifh.uni-karlsruhe.de/science/envflu/

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SHEAR LAYER

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Laser-Induced Fluorescence (LIF) VISUALIZATION OF AN AXISYMMETRIC TURBULENT JET, C. Fukushima and J. Westerweel, Technical University of Delft, The Netherlands

x

x

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Laser-Induced Fluorescence (LIF) VISUALIZATION OF AN AXISYMMETRIC TURBULENT JET, C. Fukushima and J. Westerweel, Technical University of Delft, The Netherlands

x

Turbulent Kinetic Energy (q2) Balance in a Jet

2

2222 wvu

q

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x

y

q2

<v2 > <u2 >

<w2 >

-<uv >

y

m2 /s

2

2

2222 wvu

q

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Laser-Induced Fluorescence (LIF) VISUALIZATION OF AN AXISYMMETRIC TURBULENT JET, C. Fukushima and J. Westerweel, Technical University of Delft, The Netherlands

x

Turbulent Kinetic Energy (q2) Balance in a Jet

02

22

0 vpvqyy

uuvyqv

xqu

No local accelerationsNo viscous transportPart of the shear production = 0No buoyancy production

wgxuuueuuqup

xdtdq

oj

ijiijijj

oj21 2

2

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x

y

02

22

0 vpvqyy

uuvyqv

xqu

ym2 /s

3

Gai

nLo

ss

xqu

2

yqv

2

yuuv

02 vpvq

y

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http://www.symscape.com/node/447

U0

WALL-BOUNDED SHEAR FLOW

Nominal limit of boundary layer

0.99U0

Viscous sublayer

For fully developed, bounded turbulent flow (not changing in x):

zxp

0 uwzu

viscous Reynolds

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zxp

0Function of x only Function of z only

CONSTANTS!

uwzu

z

centerline or surface

zu

Stress distribution is then LINEAR

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zzuw

xuu

0

1in boundary layer over flat plate (no press grad):

uwzu

z

zedge of boundary layer

stress is now a function of x and z

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Near the wall – Different Layers

zuu ,,, 0

http://furtech.typepad.com/

z

ū (x)

u(x,z)

0,Only involve mass dimension

Should appear together in nondimensional groups

0

* u Friction Velocity

zuuu ,,*

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zuuu ,,*

This relates 4 variables involving the dimensions of length and timeAccording to the PI THEOREM, this relationship has 4 variables and 2 dimensions

Then, only two (4 – 2) non-dimensional groups can result:

zfzuf

uu

*

*

Law of the Wall

Inner part of the wall layer, right next to the wall, is called the viscous sublayer – dominated by viscous effects

Z+ is a distance nondimensionalized by the viscous scale z*u

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*uu

*uu

z z

z (m

) = z

+ν/u

*

viscous sublayer

zu

0

zu 0gintegratin

zuu

*:onalnondimensi

buffer layer

logarithmic layer

5~z

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*uu

z

viscous sublayer

buffer layer

logarithmic layer

zfzuf

uu

*

*

outer layer

FzF

uUu

*

Velocity defect law

Law of the wall

dzdfu

zu

2*

ddFu

zu *

zfz

ddF

1

Karman constant = 0.41

Equating and multiplying times z/u*

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zfz

ddF

1

Karman constant = 0.41

Integrating: Azzf ln1

BF

ln1

From experiments: 5ln1 *

*

zu

uu 1ln1

*

z

uUu

*uu

z

Velocity distributions for theOverlap layer,Inertial sublayer,Logarithmic layer

Logarithmic velocity distribution near a boundary can also be derived from dimensional analysis

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zu

can only depend on z, and the only relevant velocity scale is u*

zu

zu *1

Czuu ln*

*zu

*uu

*

5u

*

30u

*

300u

0@0 zzu 0

* lnzzuu

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0

* lnzzuu

m005.0sm04.0

0

*

zu

0

* u

Pa20

Data from Ponce de Leon Inlet

FloridaIntracoastal Waterway

Florida