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velocityprofile
FlowControlLab,KAISTAbuSeena
Phd Student
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1 Lo lawvelocit rofilesinsmoothwallturbulent
channelflows.2) Laglawforturbulentflowsintransitionalroughpipe.
3) Reynoldsstressmodel(Sreenivasan 2005).
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Introduction
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u
uT 2
Tw
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Osborne Reynolds : Turbulent Motion can
),,('),( += tyxuyxuU
random fluctuations (u) on mean flow (u).
),,('),(
),,('),(
),,('),(
+=
+=
+=
tyxpyxpP
tyxwyxwW
tyxvyxvV
'''''
ns,fluctuatioofmeanSuch that
),,('),(
=====
+= tyxTyxTTe
0''
but
vu
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'''''
2
2
'
wuvuu
'''''
appears,resseseyno s2
Re
=
wwvwu
wvvvu
equationmomentumMean
:owc anneeve opeu y
Viscous Shear stress
:ConditionsBoundary
'' =
dx
vuyy
''
0'',0,0:Wall
==
====
u
vuvuy
(unknown)
,,y
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era ure ev ew
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"It became clear for me that it is unrealistic to hope for thecreation of a pure self-contained theory [of turbulent flows
...
we have to rely upon hypothesis obtained by processingexperimental data... I did not carry out experiment workm sel but i s ent a lot o ener on calculations andgraphical processing of data obtained by otherresearchers.
1) Boussinesq eddy viscosity model2) Prandtls mixing length model
- , .
Present Approach:Open or under-determined equations
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InnerLa er WallLaw Prandtl 1925
ViscousSheardominates
OuterLayer DefectLaw (vonKarman,1930)
TurbulentSheardominates
OverlapRegion LogLaw (Izakson1937&Millikan1939)
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elocity.friction vis/,DominatesShearViscous =
= u
y
uww
groupslessdimensionatindependen1
)dimensionstindependen3,parameters(4analysisldimensiona
,,,ParameterslDimensiona
yw
yuu ==u ++ ,
+++
= yuuLaw of the wall :
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ParameterslDimensiona
''DominatesShearTurbulent =
uU
vuw
groupsessdimensionltindependen1
)dimensionstindependen3,parameters(4analysisldimensiona
c
channelofdepthsemi,and ==
Yy
u
uUc
yuUc ==
Velocity Defect Law :
u
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OverlapRegion
Izakson(1937)&Millikan(1939)
YFuUuu =
numberReynoldslargelysufficientFor
DominatesShearTurbulentandViscousBoth
FYuy
c
== ++ 1
getweating,Differenti
Fu
or
y
+
11
Yyy=
=
++
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Lo Law :
uU
kByku
uu
=+== ++
1
ConstantKarmanvonln1
Inner log law
uRDBRUc =++= ,ln
1
DY
ku
c += ln
Skin Friction Law :
ku
Uniformly valid solution :
===
+=+= ++
lawwake-wallComposite
1)1(,0)0((1956),ColesoffunctionwakeW(Y)
,ln)()(,ln)()(
WW
DYk
YFYWk
DYk
YFyuuu
+= ++
sublayerviscoustheAbove
)()( YWk
yuuu
++= + )(ln YW
kBy
kuu
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Traditional Log Region in Overlap Domain
Innerloglaw
SemilogScale
Byk
yu += +++ ln1)(
DYk
YuU += ++ ln1
)(
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Rou hness
Lettheroughnessheightbeh
h
Thenroughnessparameter
If Equivalent to smooth wall
Viscous sub layer destroyed
Transitionally Rough wall
Major impact of the wall roughness is to perturb wall layer. Which leads to increase in wall shear stress accompanied by wall heat
transfer and mass transfer.
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LiteratureReview
Millikan(1938)proposedtwolayertheory(InnerandOuterlayer)fortransitional,fullysmoothandfullyroughpipestoobtainloglawsdependenton
k Karmanconstantandadditiveconstantdependingonroughness.
Clauser &Hama(1954) Introducetheroughnessfunction ,asan
additionaltermtosmoothwallloglaw,where
itisusefuldescriptorofsurfaceroughnesseffectonmeanvelocitypro e nt e nnerreg on
itphysicallyrepresentroughnessdominatedshiftinvelocityprofile
fromloglawofsmoothwall
t es t s ownwar ueto ncreaseo rag. theshiftisupwardduetoreductionofdrag.
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LiteratureReview
BZku
uZu +== +++ ln
1)(
Fully Rough wall Log law
Bh
Z
ku
uZu +==+
+++ ln
1)(
Log law for transitionally rough wall
BUZku
u
Zu+==
++++ ln
1
)(
Present Approach
++ =+==Z
Bu
u ,ln1
)(
)(exp += Uk
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AlternateScales
ew on mens ona roug nesssca e,
oug nesscoor natean oug nessve oc ty
Base ona ternateroug wa var a es,t e nnervar a esare e ne as
RoughnessFrictionReynoldsnoR
andRoughnessReynoldsnoRe
2
228
82
===
bbb
U
u
UU
d
dx
dp
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Power law region in Overlap Domain
Velocityprofile Velocityprofile
Innerwallvariables OuterPowerLaw
Reynoldsshearstress Reynoldsshearstress
The inner la er e uation becomes The outer la er e uation becomes
Matching
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Lo Law :Inner log law , k = vonkarman conatantB
ku
uu +==+
ln1
)(
Skin Friction Law :
Composite velocity profile solutions:
W(Y) = wake function of Coles(1956), with BC W(0)=0 and W(1) = 1and
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Nikuradse Sand Grain Roughness data (inflectional roughness)
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Shockling Superpipe data (with machine honed surface)
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FrictionFactor:
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CommercialandSandGrainRoughness
Colebrooks Equation(commercialroughness)
+=
f
D
f Re
51.2
7.3log2
1
++
===
+=
BBBBk
hkU
FF
5.8,5.5)],(exp[
)1ln(1
ForInflectionalroughness(Loselevich andPilipenko)
++= h 1
)25.2/(ln),(sin)ln5.8( 1 ++
+ =+= hqqhkBU .n
+=
jh ex1
j=0 forColebrooksmonotonicroughness
j=11forinflectionalroughness
+h
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ConclusionA) Openequations Functionalapproach
1) The open momentum equation in fully developed turbulent channel flowconsists of two la ers, inner la er near the wall and outer la er awafrom the wall. The matching of the inner and outer layer in overlap
region gives velocity profiles in terms of log law.
=Zinnervariable, theroughnessfrictionReynoldsnumber
and theroughnessReynoldsnumber.
3 The velocit rofile in transitional wall rou hness inner variable
/RR =
Re/Re =
, isuniversalforalltypesofwallroughness,in
contrasttotraditionalwallvariableZ+orZ/h.
4 The friction factor vs rou hness Re nolds number Re is also
+=Z
universal,explicitlyindependentofwallroughness.
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ClosureModel:
Lo arithmicEx ansionsforRe noldsStress
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ClosureModel:ReynoldsShearStress
Sreenivasan,K.R.andBershadskii(2006,JFMVol554pp477498):
ProposedReynoldsShearStressModel
2=
( )2/1
87.1 Rym
m
=+
++
Re nolds momentum e uation in a channel
Maxima occurs at
+
+
+
+ =+ yRdy
du 11
1111 ,1)]/[ln()(where
)2()]2/()([const
kpkkpeyyppyg
Ryygyu
omo =+=+=
+=
+++
++++
o ut on or ve oc ty str ut on:
.Reas1andenough,highisitleast whenatnumber,
ReynoldsoftindependenbetoandConstants:Assumption 1
kk
.
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PresentAnalysisonClosureModelforReynoldsShearStress
[ ]kRy
yyk
mm
m
==
+=
++
++
,
...........)]/[ln(1 21Reynolds Shear stress:
Maxima occurs at
givesat0 Ry == ++
221
1 )]/[ln()]/[ln()( RyR m == +
Boundary conditions (imposed):
,1)]/[ln()(where
)]2/()([const
kpkkpeyyppyg
Ryygyu
=+=+=
+= ++++
Solution for velocity distribution
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Velocity Distribution
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Conclusion
1. TheclosuremodelofReynoldsshearstressintermsoflogarithmsofnon
dimensionalverticalcoordinateappearstoworksroughlyfory+ >10.
. eve oc y ncoor na es u+ y+ +y+ , y+ area so ngoo agreemen
withthedataalmostallthewaytocenterline.3. But velocityprofile(u+,y+) showappreciabledepartureintheoverlapregion,
.
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ThankYou
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References
Afzal,N.andAbuSeena 2007,AlternateScalesforTurbulentFlowinTransitionalRoughPipes:UniversalLogLaws J.FluidEngg,Vol 129,pp8090.
Millikan,C.B.,1938,ACriticalDiscussionofTurbulentFlowinChannelsandCircularTubes,Proc.5thInt.
Cong.Appl.Mech.Cambridge,J.P.denHartog andH.Peters,eds.,Wiley/ChapmanandHall,NewYork
, . .
Clauser,F.H.,1954,TurbulentBoundaryLayersinAdversePressureGradients,J.Aeronaut.Sci.,21,pp.91
108.
Hama,F.R.,1954,BoundaryLayerCharacteristicsforRoughandSmoothSurfaces,TransSocietyofNaval
, , . .
Abe,K.,Matsumoto,A.,Munakata,H.,andTani,I.,1990,DragReductionbySangGrainRoughness,In
StructureofTurbulenceandDragReduction,A.Gyr,ed.,SpringerVerlag,Berlin,pp.341348.
Nikuradse,J.,1933,LawsofFlowinRoughPipe,VI,Forchungsheft N361,EnglishtranslationNACATM1292,
1950.
Shockling,M.A.,2005,TurbulentFlowinRoughPipe,MSEthesis,PrincetonUniversity.
Shockling,M.A.,Allen,J.J.,andSmits,A.J.,2006,RoughnessEffectsinTurbulentPipeFlow,J.FluidMech.,
564,pp.267285.
Colebrook,C.F.,1939,TurbulentFlowinPi esWithParticularReferencetotheTransitionRe ionBetweenthe
SmoothandRoughPipeLaws,J.Inst.
Civ.
Eng,11,pp.133156.
Allen,J.J.,Shockling,M.A.,andSmits,A.J.,2005,EvaluationofaUniversalTransitionalResistanceDiagram
forPipesWithHonedSurfaces,Phys.Fluids,17,pp.121702.
Abe,H.,Kawamura,H.,andMatsuo,Y.,2001,DirectNumericalSimulationofaFullyDevelopedTurbulent
ChannelFlowWithRespecttoReynolds Number,J.FluidsEng.,123,pp.382393.
Afzal,N.,1982,FullyDevelopedTurbulentFlowinaPipe:AnIntermediateLayer,Ing.Arch.,53,pp.355377.