A revised model.docx
《A revised model.docx》由会员分享,可在线阅读,更多相关《A revised model.docx(22页珍藏版)》请在冰豆网上搜索。
![A revised model.docx](https://file1.bdocx.com/fileroot1/2022-11/30/50f92aee-7986-4bd5-be15-4f062c3daece/50f92aee-7986-4bd5-be15-4f062c3daece1.gif)
Arevisedmodel
Naturalconvectiveboundary-layerflowofananofluidpastavertical
plate:
A.V.Kuznetsov
a,
*,D.A.Nield
b
a
DepartmentofMechanicalandAerospaceEngineering,NorthCarolinaStateUniversity,CampusBox7910,Raleigh,NC27695-7910,USA
b
DepartmentofEngineeringScience,UniversityofAuckland,PrivateBag92019,Auckland1142,NewZealand
articleinfo
Articlehistory:
Received5May2013
Receivedinrevisedform
23July2013
Accepted17October2013
Availableonline4December2013
Keywords:
Nanofluid
Brownianmotion
Thermophoresis
Naturalconvection
Boundarylayer
Verticalplate
abstract
Theproblemofnaturalconvectiveboundary-layerflowofananofluidpastaverticalplateisrevisited.
Themodel,whichincludestheeffectsofBrownianmotionandthermophoresis,isrevisedsothatthe
nanofluidparticlefractionontheboundaryispassivelyratherthanactivelycontrolled.Inthisrespectthe
modelismorerealisticphysicallythanthatemployedbypreviousauthors.
_2013ElsevierMassonSAS.Allrightsreserved.
1.Introduction
ThemodelforananaofluidincludingtheeffectsofBrownian
motionandthermophoresis,introducedbyBuongiorno[1],was
appliedbyKuznetsovandNield[2]totheclassicalproblemstudied
byPohlhausen,KuikenandBejan[3e6],namelyconvective
boundarylayerflowpastaverticalplate.Intheirpioneeringpaper
KuznetsovandNield[2]employedboundaryconditionsonthe
nanoparticlefractionanalogoustothoseonthetemperature.Inthis
notetheproblemisrevisitedandaboundaryconditionthatismore
realisticphysicallyisapplied.Itisnolongerassumedthatonecan
controlthevalueofthenanoparticlefractionatthewall,butrather
thatthenanoparticlefluxatthewalliszero.Thischangenecessitatesarescalingoftheparametersthatareinvolved.
2.Analysis
ThefollowinganalysiscloselyfollowsthatinRef.[2]andsois
describedbrieflyhere.Atwo-dimensionalproblemisconsidered.A
coordinateframeinwhichthex-axisisalignedverticallyupwards
isutilized.Averticalplateisaty¼0.Weassumethataty¼0the
temperatureTtakestheconstantvalueTw.Thefluxofthenanoparticlefractionaty¼0istakentobezero.Theambientvalueof
temperatureisTNandtheambientvalueofthenanoparticlefractionisfN;theambientvaluesareattainedataninfinitedistance
fromthewall.
WeusedtheOberbeck-Boussinesqapproximation.Thegoverningequationsexpressingtheconservationoftotalmass,momentum,thermalenergy,andnanoparticlesare,respectively:
V$v¼0;
(1)
rf
_
vv
vt
þv$Vv
_
¼_VpþmV
2
vþ
h
frp
þð1_fÞ
_
n
rf
ð1_bðT_TNÞÞ
oi
g;
(2)
ðrcÞ
f
_
vT
vt
þv$VT
_
¼kV
2
TþðrcÞ
p
½DBVf$VTþðDT=TNÞVT$VT_;
(3)
vf
vt
þv$V4¼DBV
2
fþðDT=TNÞV
2
T:
(4)
InEqs.
(1)e(4)thefieldvariablesarethevelocityv[wewrite
v¼(u,v)],thetemperatureTandthenanoparticlevolumefraction
*Correspondingauthor.
E-mailaddresses:
avkuznet@ncsu.edu(A.V.Kuznetsov),d.nield@auckland.ac.nz
(D.A.Nield).
ContentslistsavailableatScienceDirect
InternationalJournalofThermalSciences
journalhomepage:
1290-0729/$eseefrontmatter_2013ElsevierMassonSAS.Allrightsreserved.
http:
//dx.doi.org/10.1016/j.ijthermalsci.2013.10.007
InternationalJournalofThermalSciences77(2014)126e129
f.Also,rfisthedensityofthebasefluidandm,kandbarethe
viscosity,thermalconductivityandvolumetricexpansioncoefficientofthenanofluid,andrPisthedensityoftheparticles.We
denotedthegravitationalaccelerationbyg.InEqs.(3)and(4)the
coefficientsDBandDTaretheBrowniandiffusioncoefficientandthe
thermophoreticdiffusioncoefficient,respectively,eachnondimensionalizedintermsoftheambientvalueofthetemperature.Itisbeingassumedthetemperaturedoesnotvarymuchfrom
theambienttemperature,andsoDBandDTmayeachbetreatedasa
constant.
Eqs.
(1)e(4)mustbesolvedsubjecttothefollowingboundary
conditions:
u¼v¼0;T¼Tw;DB
vf
vy
þ
DB
TN
vT
vy
¼0aty¼0;(5a,b,c)
u¼v¼0;T/TN;f/fNasy/N:
(6a,b,c)
Asteadystateflowisconsidered.Eq.(5c)isastatementthat,
withthermophoresistakenintoaccount,thenormalfluxofnanoparticlesiszeroattheboundary[7,8].
WeusedtheOberbeck-Boussinesqapproximation.Wealso
madeanassumptionthatthenanoparticleconcentrationisdilute.
Usingasuitablechoiceforthereferencepressure,welinearizedthe
momentumequationandrecastEq.
(2)asfollows:
rf
_
vv
vt
þv$Vv
_
¼_VpþmV
2
vþ
h_
rp_rfN
ðf_fNÞ
þð1_fNÞrfNbðT_TNÞ
i
g:
(7)
Basedonascaleanalysis,wenowemploythestandard
boundary-layerapproximation,andexpressthegoverningequationsas
vu
vx
þ
vv
vy
¼0;(8)
vp
vx
¼m
v
2
u
vy
2
_rf
_
u
vu
vx
þv
vu
vy
_
þ
h
ð1_iNÞrfNbgðT_TNÞ
_
_
rp_rfN
gðf_fNÞ
i
;(9)
vp
vy
¼0;(10)
u
vT
vx
þv
vT
vy
¼aV
2
Tþs
"
DB
vf
vy
vT
vy
þ
_
DT
TN
__
vT
vy
_2
#
;(11)
u
vf
vx
þv
vf
vy
¼DB
v
2
f
vy
2
þ
_
DT
TN
_
v
2
T
vy
2
;(12)
where
a¼
k
ðrcÞ
f
;s¼
ðrcÞ
p
ðrcÞ
f
:
(13)
Weusedcross-differentiationtoeliminatepfromEqs.(8)and
(9).Wealsointroducedastreamfunctionjdefinedby
u¼
vj
vy
;v¼_
vj
vx
:
(14)
Eq.(8)isnowsatisfiedidentically.
Thisleavesuswiththefollowingthreeequations:
vj
vy
v
2
j
vxvy
_
vj
vx
v
2
j
vy
2
_n
v
3
j
vy
3
¼ð1_fNÞrfNbgðT_TNÞ
_
_
rp_rfN
gf(15)
vj
vy
vT
vx
_
vj
vx
vT
vy
¼aV
2
Tþs
"
DB
vf
vy
vT
vy
þ
_
DT
TN
__
vT
vy
_2
#
;(16)
Nomenclature
DBBrowniandiffusioncoefficient
DTthermophoreticdiffusioncoefficient
frescalednanoparticlevolumefraction,definedbyEq.
(20)
ggravitationalaccelerationvector
kthermalconductivity
LeLewisnumber,definedbyEq.(28)
Nrbuoyancyeratioparameter,definedbyEq.(25)
NbBrownianmotionparameter,definedbyEq.(26)
Ntthermophoresisparameter,definedbyEq.(27)
NuNusseltnumber,definedbyEq.(31)
NurreducedNusseltnumber,Nu/Rax
1/4
PrPrandtlnumber,definedbyEq.(24)
ppressure
q
00
wallheatflux
RaxlocalRayleighnumber,definedbyEq.(18)
sdimensionlessstreamfunction,definedbyEq.(20)
Ttemperature
Twtemperatureattheverticalplate
TNambienttemperatureattainedasytendstoinfinity
vvelocity,(u,v)
(x,y)Cartesiancoordinates(x-axisisalignedvertically
upwards,plateisaty¼0)
Greeksymbols
athermaldiffusivity
bvolumetricexpansioncoefficientofthefluid
hsimilarityvariable,definedbyEq.(19)
qdimensionlesstemperature,definedbyEq.(20)
mdynamicviscosityofthefluid
nkinematicviscosity,m/rfN
rffluiddensity
rpnanoparticlemassdensity
(rc)fheatcapacityofthefluid
(rc)peffectiveheatcapacityofthenanoparticlematerial
sparameterdefinedbyEq.(13),(rc)p/(rc)f
fnanoparticlevolumefraction
fNambientnanoparticlevolumefractionattainedasy
tendstoinfinity
jstreamfunction,definedbyEq.(14)
A.V.Kuznetsov,D.A.Nield/InternationalJournalofThermalSciences77(2014)126e129127
vj
vy
vf
vx
_
vj
vx
vf
vy
¼DB
v
2
f
vy
2
þ
_
DT
TN
_
v
2
T
vy
2
:
(17)
Eq.(15)wasderivedbyintegrationwithrespecttoy;theuse
wasalsomadeoftheboundaryconditionsatinfinity.InEq.(15)
n¼m/rfN.
ThelocalRayleighnumberRaxwasdefinedby
Rax¼
ð1_fNÞbgðTw_TNÞx
3
na
;(18)
andthesimilarityvariablewasdefinedby
h¼
y
x
Ra
1=4
x
:
(19)
Thesimilarityvariablewaschosenonthebasisofscaleanalysis.
Ourreviewshowsthatmostnanofluidshavelargevaluesforthe
LewisnumberLe.ForthisreasonweconcentrateonthecaseLe>1.
Wealsoassumethatheattransfer,ratherthanmasstransfer,drives
theflow.Intermsofourmodel,thisimpliesthatthebuoyancye
ratioparameterNrdefinedbyEq.(25)belowissmallincomparison
withunity.ThisalsoimpliesthattheLewisnumberLedefinedby
Eq.(28)belowisgreaterthanunity.
Thedimensionlessvariabless,q,andfwereintroducedbythe
followingequations
sðhÞ¼
j
aRa
1=4
x
;qðhÞ¼
T_TN
Tw_TN
;fðhÞ¼
f
fN
:
(20)
WesubstitutedthequantitiesdefinedbyEq.(20)intoEqs.(15)e
(17)andobtainedthefollowingordinarydifferentialequations
s
000
þ
1
4Pr
_
3ss
00
_2s
02
þq_Nrf¼0;(21)
q
00
þ
3
4
sq
0
þNbf
0
q
0
þNtq
02
¼0;(22)
f
00
þ
3
4
Lesf
0
þ
Nt
Nb
q
00
¼0:
(23)
ThefivedimensionlessparametersinEqs.(21)e(23)are
Pr¼
n
a
;(24)
Nr¼
_
rp_rfN
fN
rfNbðTw_TNÞ
;(25)
Nb¼
ðrcÞ
pDBfN
ðrcÞ
fa
;(26)
Nt¼
ðrcÞ
pDT
ðTw_TNÞ
ðrcÞ
faTN
;(27)
Le¼
a
DB
:
(28)
HereNristhebuoyancyratio,NbistheBrownianmotion
parameter,Ntisthethermophoresisparameter,andLetheLewis
number.
WesolvedEqs.(21)e(23)subjecttothefollowingboundary
conditions:
Ath¼0:
s¼0;s
0
¼0;q¼1;Nbf
0
þNtq
0
¼0;(29a,b,c)
Ash/N:
s
0
¼0;q¼0;f¼0:
(30a,b,c)
ForthecasewhenNr,NbandNtareallequaltozero,thereare
justtwoindependentvaluablesinvolvedinEqs.(21)and(22)
(namelysandq).Theboundary-valueproblemforthesetwovariablesreducestotheclassicalPohlhausen-Kuiken-Bejanproblem,
whiletheboundaryvalueproblemforfthenbecomesill-posedand
hasnophysicalsignificance.
WedefinedtheNusseltnumberNuas
Nu¼
q
00
x
kðTw_TNÞ
:
(31)
Hereq
00
isthewallheatflux.ThereducedNusseltnumber
Nu/Rax
1/4
whichwedenotedbyNur,isfoundas_q
0
(0).The
readerwillnotethatthedimensionlessmassfluxrepresented
byaSherwoodnumberShisnowidenticallyzero.
3.Resultsanddiscussion
Asabaselineforcomparison,wefirstpresentinTable1some
resultsforthelimitingcaseofaregularfluid.Wethenpresentthe
resultsofourinvestigationoftheeffectoftheparametersNr,Nb
andNtonNur,forvariousvaluesofPrandLe.
In