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2.6HeterogeneousCatalysis&Adsorption2.6.1HeterogeneouscatalysisForasolidcatalyzedreaction
thereactionmechanismmaybeA+BR(2.60)A+BAB+R+RcatalystadsorptionreactiondesorptiondiffusiondiffusionsurfacereactionactivesiteadsorbedmoleculesTheelementarystepsofsurfacereactionareassumedasadsorptionA+A(2.61a)adsorptionB+B(2.61b)reaction
A+BR+(2.61c)desorptionRR+(2.61d)2.6.2Adsorptionanddesorptionphysicaladsorptionbyintermolecularforces,multilayer
atlowertemperaturechemicaladsorptionbychemicalbond,monolayer
athightemperatureloweractivationenergyheatofadsorptionO(heatreaction)1.Idealadsorption
Basicassumptions:(1)thesurfaceishomogeneousforadsorption;(2)theintermolecularforcesbetweenadsorbedmoleculesarenegligible;(3)itisamonolayeradsorption.LangmuiradsorptionmodelAtthesurface,wherekaandkdareadsorptionanddesorptionrateconstant,respectively.adsorptionrate:
ra=ka
pA(1A)(2.62)desorptionrate:
rd=kdA
(2.63)whereAisthefractionofcoverageofA.A+A
kakdThenetadsorptionrateis
r=ka
pA(1A)
kdA
Atdynamicequilibrium,r=0,sothatka
pA(1A)=
kdAThefractionofcoverageis(2.64)where
KA=ka
/kd
isreferredtoasadsorptionequilibriumconstant.Langmuiradsorptionisotherm
kaand
kd
areusuallyexpressedas
ka
=ka0exp(Ea/RT)
kd
=kd0exp(Ed/RT)whereEaandEdareactivationenergyofadsorptionanddesorption,respectively.(2.66)whereq=Ed
Ea,heatofadsorption.Fortheadsorptionofmkindsofmolecules,thefractionofcoverageof
i
isthefractionofvacancyis(2.72)(2.73)whichwillbederivedlater.Ifanadsorbedmoleculeisdissociatedintoatoms,rateofadsorption:
ra=ka
pA(1A)2
rateofdesorption:
rd=
kdA2
fractionofcoverage:
A2+22A
kakd(2.74)Langmuirdissociativeadsorptionisotherm2.RealadsorptionThesurfaceisinhomogeneousforadsorption,
EaandEd
dependon.Theintermolecularforcesbetweenadsorbedmoleculesaresignificant.Itmaybeassumedthat
Ea=Ea0+A
(2.75)
Ed=Ed0
A
(2.76)wheresuperscript0referstozerocoverage,andareconstants.Theheatofadsorptionis
q=q0
(+)A(2.77)whereq0=Ed0
Ea0.Idealsurface:
ra=ka
pA(1A)(2.62)
rd=kdA
(2.63)Non-idealsurface:rateofadsorption:
ra=ka0
pAexp(A/RT)rateofdesorption:
rd=kd0exp(A/RT)A+A
kakdNon-idealsurface:
ra=ka0
pAexp(A/RT)rd=kd0exp(A/RT)Atadsorptionequilibrium,(2.78)whereK0=ka0/kd0.
The
adsorptionisothermisvalidformediumcoverage.Otherassumptionsotherisotherms.2.7HeterogeneousCatalyticKinetics2.7.1Importantapproximations
Steady-stateapproximation:foraseriesofreactionsteps,theconcentrationofintermediateisnotafunctionoftime,sothattheratesofallstepsareequal.
Ratedeterminingstepistheonewiththeslowestrateamongthesteps,whichdeterminestheoverallrate,andotherstepsareinequilibriumstate.2.7.2RateequationofheterogeneouscatalysisExample:A+BR(2.60)adsorptionA+A(2.61a)adsorptionB+B(2.61b)reaction
A+BR+
(2.61c)desorptionRR+(2.61d)with(1)forreactioncontrolling
Theoverallrateofreactionequalstherateofreaction,
r=k1AB
k2RV(2.82)Otherstepsreachequilibrium,sothatA:
kaA
pAV
kdAA=0B:
kaB
pBV
kdBB=0
R:
kaR
pRV
kdRR=0k1k2
A+BR+
(2.61c)Fractionofcoverage:
A=KA
pAV
(2.83)
B=KB
pBV(2.84)
R=KR
pRV(2.85)Kadsorptionequilibriumconstant,p
partialpressure.Since
A+B
+R+V=1(2.73)ThefractionofcoverageofcomponentiisNote:
includesalladsorbedcomponentswhethertheyreactornot.(2.72)Theoverallreactionrate
equationiswhere
k=k1KAKB
,apparentrateconstant;(2.87)apparentchemicalequilibriumconstant.If<<1,reactioninhomogeneousphase.(2)foradsorptionofAcontrolling
TheoverallrateofreactionequalstherateofadsorptionofA,
r=kaA
pAV
kdAA
(2.88)Otherstepsreachequilibrium,e.g.,reaction
(2.89)whereKsistheequilibriumconstantofsurfacereaction,BandRareexpressedbyEqs.(2.84)and(2.85).From A+B+R+V
=1,weobtainsotheoverallreactionrateequationis(2.92)(3)fordesorptionofRcontrolling
TheoverallrateofreactionequalstherateofdesorptionofR,
r=
kdRR
kaRpRV
(2.93)Theoverallreactionrateequationis(2.94)wherek’=kdRKsKAKB
.Rateequationsarealloftheform
kinetictermapparentrateconstantdrivingforcedisplacementfromequilibriumresistancetermadsorptiontermForidealsurface,theyarehyperbolictype.rateofreaction=(kineticterm)(drivingforce)resistancetermStepsforidealsurfaces:(1)assumethereactionmechanism;(2)theoverallrateequalstherateof
controllingstep,r=f(pi,i,V,…);(3)otherstepsinequilibriumleadto
i;(4)findV;(5)withiandV,r
=f(pA,pB,…)
Ifthereisnoratecontrollingstepornon-controllingstepisirreversible,thesteady-stateapproximation
isused.
Example2.7Idealadsorption
Cyclohexaneisproducedfrombenzeneandhydrogenwithanickelcatalyst,C6H6+3H2C6H12
Thereactionmechanismisassumedas(1)H2+222H2
(2)C6H6+1C6H61(3)C6H61+H2
C6H71+2(4)C6H71+H2C6H81+2
…………(8)C6H111+H2
C6H12+1+2
ratecontrollingstepweakadsorptionSolution:
Fortheirreversiblereaction,
r=
ks1B2H
(A)ForthedissociativeadsorptionofH2,(C)Fortheadsorptionofbenzene,(B)overallrateequation.Example2.8RealadsorptionThecatalyticreactionforsyntheticammoniaisN2+3H22NH3Thereactionmechanismisassumedas(1)N2+2
2N(2)H2+22H(3)N+HNH+(4)NH+HNH2+(5)NH2+HNH3+(6)NH3NH3+2N+3H22NH3+2
adsorptioncontrolSolution:
Theoverallrateofreactionisr=kapN
exp(N/RT)
kd
exp(N/RT)whereinwhichistheequilibriumpartialpressureofN2,whichmaybeobtainedfrom2N+3H22NH3+2
k1k2(B)fromEq.(2.78)Whenitreachesequilibrium,wehavewherepAandpHarethepartialpressureofNH3andH2.Theequilibriumconstantis(C)(=1/2)2N+3H22NH3+2
k1k2(B)Therateequationofreactioniswhichisapowerfunction.Exercises:Chap.2:14,15,16,17
(D)Fordifferentreactionmechanism,differentrateequationmaybeobtained,andshouldbeverifiedexperimentally.Thesimplestformofempiricalequationsisthepowerfunction,Inprinciple,theformofempiricalrateequationshouldbeassimpleaspossible.Theparametersaredeterminedexperimentally.2.8DeterminationofKineticParameters
e.g.,rateconstant,orderofreaction,
equilibriumconstantsofreaction,adsorptionanddesorption,
activationenergy,etc.2.8.1IntegralmethodIntegratetherateequationdeterminetheparametersfromexperimente.g.,
(2.95)Theintegrationis(2.96)(1)plotleastsquaredmethodTheexperimentaldata(cA
t)areuseddirectly,buttheorder
isassumed.(2.96)(1)(1)k0tlinearization
2.8.2DifferentialmethodLinearization:lnrA=
lncA+ln
kThedata(cA
t)arechangedto
rA,buttheorder
isobtainedfromplotorcalculationdirectly.(2.95)e.g.,0lncAlnrAab2.8.3Datafitting1.Linearregression
Whenthedataappearsastraightline,
y=ax+
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