Electroactivity of Pt-Ru-polyaniline composite catalyst-electrodes prepared by electrochemical depos
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SolidStateIonics178(2008)1915–
1921
/locate/ssi
ElectroactivityofPt–Ru/polyanilinecompositecatalyst-electrodes
preparedbyelectrochemicaldepositionmethods
SeokKima,Soo-JinParkb,
a
AdvancedMaterialsDivision,KoreaResearchInstituteofChemicalTechnology,P.O.Box107,Yuseong,Daejeon305-600,SouthKorea
b
DepartmentofChemistry,InhaUniversity,253,Nam-gu,Incheon402-751,SouthKorea
Received6September2007;receivedinrevisedform17December2007;accepted21December2007
Abstract
TheelectrochemicaldepositionofPt–Runanoparticlesonconductingpolymersupportsandcarbonsupports,aswellastheirelectro-catalyticactivities,wereinvestigated.Pt–Rucatalystsof3–8nmaveragesizeweregrownonsupportsbystep-potentialplatingmethods.Thecatalysts'loadingcontentswereenhancedbyincreasingtheplatingtimeofthedepositionmethod.Polyanilineandcarbonblacks(CBs)wereselectedandcomparedascatalystsupports.TheparticlesizesandmorphologicalstructuresofthePt–Ru/supportcatalystswereevaluatedusingX-raydiffraction(XRD)andtransmissionelectronmicroscopy(TEM).TheelectrochemicalbehaviorsofthePt–Ru/supportcatalystsformethanoloxidationwereinvestigatedaccordingtotheircharacteristiccurrent-voltagecurvesandchronoamperometryinamethanolsolution.Asaresult,theelectrochemicalactivitywasenhancedwithincreasedplatingtime,reachingthemaximumat24min,andthendecreased.Thespecificcurrentdensityforthepolyaniline-supportedcatalystswashigherthanthatfortheCBs-supportedones.Theenhancedcatalyticactivitywasrelatedtothehigherelectricalconductivityofthepolyaniline,theincreasedelectrochemicalsurfaceareaofcatalysts,orthehigheriondiffusionbehaviours.©2008ElsevierB.V.Allrightsreserved.
Keywords:Catalyst-electrodes;Platingmethods;Electroactivity;Supportmaterials;Fuelcells
1.Introduction
Directmethanolfuelcells(DMFCs)areanattractivepor-tablepowersourceowingtotheirhighenergydensity,easyfuelhandling,andalowoperatingtemperature[1–4].However,DMFCsentailsomeserioustechnicalobstacles.Oneistherelativelyslowkineticsofthemethanoloxidationreactionatananode,whichleadstohighover-potentials[5].Platinum(Pt)hasahighactivityformethanoloxidation,andhasbeenusedinanodeelectrocatalystsformanyyears[6–8].However,thePtelectrocatalystwillbepoisonedbyintermediatesofmethanoloxidation,suchasCO.Sincethemid-1970s,topromotemethanolelectro-oxidationbyPt,thecatalystsurfacehasbeenmodifiedbytheadditionofasecondmetaltoPt[9–11].TheresultingPt–Rubinarymetalliccatalystiscommonlyacceptedasthebestelectrocatalystformethanoloxidation[12–15].The
Correspondingauthor.Tel./fax:+82328608438.E-mailaddress:sjpark@inha.ac.kr(S.-J.Park).
0167-2738/$-seefrontmatter©2008ElsevierB.V.Allrightsreserved.doi:10.1016/j.ssi.2007.12.074
otherissueinDMFCsisthemethanolcrossoverfromanodetocathodeacrossthemembrane.Itiswellknownthatmethanolcrossoverlowersfuelutilizationandcausescathodeover-potential[16–19].
Pt–Rucatalystscanbepreparedbyanelectrochemicalplatingmethodaswellasaconventionalchemical-reductionmethod[20–22].Recently,electrochemicaldepositionofmetalcatalystshasbeenreceivingmoreandmoreattentionduetoadvantagessuchasitshighpurityofdeposits,simpledepositionprocess,andeasycontroloftheloadingmass.Byapplyingaspecificcurrentforashorttime,andthenrepeatingtheprocessduringelectrodeposition,eachcycleofthisprocesscangeneratenewmetalparticles[23].Therefore,bycontrollingthemag-nitudeofthecurrentorpotential,nanoparticlescanbealteredinsizeandstructure[24].Beside,thedevelopmentofasup-portmaterialisessentialtominimizingnoblemetalloadingandachievingoptimumcatalyticperformance[25–30].Carbonmaterialsarewidelyusedassupportmaterials.Althoughcarbonblacks(CBs)arethemostcommerciallyusedcarbonsupportmaterials,differentkindsofcarbonnanotubes,graphiticcarbon
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nanofibers,andorderedmesoporouscarbonshaverecentlybeeninvestigated[31–34].
Thesizeandloadingcontentofcatalystparticlesonthesubstratedeterminethecatalysts'performanceasanelectrodematerial.Ithasbeenreportedthataneffectivedispersionofcatalystparticlescausesadecreaseinsurfacepoisoning.Dif-ferentsubstratesforcatalystparticleshavebeentried,withtheaimofimprovingtheefficiencyofmethanolelectro-oxidation.Conductingpolymerscanbeusedassuitablehostmatricesfordispersingmetallicparticles.Conductingpolymer/metal-nano-particlescompositespermitafacileflowofelectronicchargesthroughthepolymermatrixduringtheelectrochemicalprocess.Additionally,electricalconductingpolymersprovidealowohmicdropofelectrontransferbetweenthemetalcatalystandthesubstrates.Also,metallicparticlescanbedispersedintothematrixofthesepolymers.Bycombiningconductingpolymersandmetalparticles,itisexpectedthatnovelelectrodeswithhigherspecificsurfaceareasandenhancedelectrocatalyticac-tivitiescouldbeprepared.
Recently,Y.E.Sungetal.proposedthatPt–Runanoparti-cles/electricalconductingpolymernanocompositesareeffectiveasanodecatalysts[35].Atthattime,theelectricalconductivityofpolymerswasrelativelylowcomparedwithamorphouscar-bon,andsyntheticmethodswerelimitedtoelectrochemicalpolymerizationfromnonaqueoussystems.Inpreviousstudies[36,37],metalparticlescouldbehomogeneouslydispersedonpolyanilinefilmbyconstantpotentialelectro-platingtechni-ques.However,inourstudy,step-potentialplatingmethodswereutilizedtoobtainasmallersizeandabetterelectrochem-icalactivity.
Theaimofthisstudywasnotonlytoimproveanelectricalconductivityandaneffectivesurfaceareaofcatalystelectrodesusingelectricalconductivity-enhancedpolyanilineasacatalystsupport,butalsotocontrolthesizeandloadinglevelofPt–Ruparticlesbythesteppotentialplatingmethod.Itisexpectedthatwell-dispersedcatalystsonconductingpolymerscanleadtobetterPtutilizationandanimprovementofthecatalyticactivityinmethanoloxidation.2.Experimental2.1.Supportmaterials
CBsandpolyanilinewereusedasasupportforthemetalcatalysts.TheCBsof24nmaverage 1particlesize,andhavingaDBPadsorptionof153(cc-100g)andaspecificsurfaceareaof112(m2g 1),weresuppliedbyKoreaCarbonBlackCo.Polyanilinepowderwassynthesizedchemicallybyoxidativepolymerizationofanilineinanaqueousacidicsolution[38–40].Theaniline(8.4g,0.09mol;Aldrich),distilledthreetimesbeforeuse,wasdissolvedin300mLofaqueoussolutioncontaining0.09moldodecylbenzenesulfonicacid(DBSA)below5°C,andanaqueoussolution(100mL)of0.06molammoniumperoxydisulfate,(NH4)2S2O8,wasaddedwithvigorousstirring,overaperiodof30min.Themixturewasstirredcontinuouslyfor24h.Theprecipitatewascollectedafterpouringmethanolandbyfiltration,andthenwashedwithwaterandmethanolthreetimes.
Theresultingpowderwasdriedunderadynamicvacuumat40°Cfor2days.TheDBSA-dopedpolyanilinewasconfirmedbymeasuringtheelectricalconductivity(~80S/cm).Theconduc-tivityofCBswas0.7S/cm.PANIandCBspellets,fabricatedbycompressing7PANIandCBspowderunderthepressureof5.0×10kg/m2atroomtemperature,weremeasuredforcon-ductivityusingthefour-probemethod.
2.2.ElectrodepositionofPt–RunanoparticlesonsupportElectrodepositionofPt–RunanoparticlesonsupportwasinvestigatedusinganAutolabwithaPGSTAT30electroche-micalanalysisinstrument(EcoChemieB.V.;Netherlands).Thesolidprecursorschloroplatinicacid(H2PtCl4,Aldrich)andrutheniumchloride(RuCl3,Aldrich)wereusedwithoutpuri-fication.Astandardthree-electrodecellwasemployed.Thesupportmaterialsmixedwith10%NafionPerfluorosulfonatedion-exchangeresin(Aldrich)solutionwasdroppedontotheglassycarbonelectrodeasaworkingelectrode.APtwireasthecounterelectrodeandKCl-saturatedAg/AgClasthereferenceelectrodewereused,respectively.Pt–Runanoparticleswere,bysteppotentialplatingmethod,electrodepositedontheCBandpolyanilinecatalystelectrodesfromdistilledwatersolutioncontainingrutheniumchlorideandchloroplatinicacid.Inthedepositionsolution,theconcentrationofPtandRuwas20mM.Apotentialfunctiongeneratorwasusedtocontrolboththesteppotentialvalueandtheintervaltime.ThepotentialwaveformofthedepositionisshowninFig.1.Thecatalystswerecycledintherangeof 0.3Vto 0.8V(V1andV2)withanintervaltime(t1andt2)of0.1s.Theelectrocatalystswerepreparedbychangingtheplatingtime.
2.3.Physicalmeasurements
Transmissionelectronmicrographs(TEM)ofthecatalystsamplesweretakenusinga200,000×magnification
transmission
Fig.1.Step-potentialplatingmethodshowingparametersofappliedpotentialandintervaltime.
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Fig.2.X-raydiffractionpatternsofPt–Ru/CBscatalystspreparedfordifferentplatingtimesof(a)6,(b)12,(c)24,and(d)36
min.
electronmicroscopewithaspatialresolutionof1nm.Beforetakingtheelectronmicrographs,thecatalystsampleswereultrasonicallydispersedinisopropylalcohol,andadropoftheresultantdispersionwasdepositedanddriedonastandardcopper-gridcoatedwithapolymerfilm.Theappliedvoltagewas100kVforthecatalysts.
AnXRDanalysiswascarriedoutonthecatalyststhatwerepreparedfromdifferentconditions,bymeansofaRigakuD/MAX-ШBX-RaydiffractometerusingaCuKαsourceoper-atingat45kVand100mA.1TheXRDpatternswereplottedatascanningrateof4°min withanangularresolutionof0.05°for2θscans.X-raydiffractogramswereobtainedfor2θvaluesvaryingbetween30°and85°.TheaveragecrystallinesizesoftheparticlesweredeterminedfromtheX-raydffractograms,usingtheScherrerEq.(1)[41].L¼
0:9k
B2hcoshmax
ð1Þ
whereλistheX-raywavelength(1.54056ÅfortheCuKαradiation),B2θisthewidthofthediffractionpeakathalf-height,andθmaxistheangleatthepeakmaximumposition.
Fig.3.X-raydiffractionpatternsofPt–Ru/polyanilinecatalystspreparedfordifferentplatingtimesof(a)6,(b)12,(c)24,and(d)36min.
Table1
MeansizeandloadingcontentsofPt–Ru/CBscatalystsPlatingtimeCrystallinesizeParticlesizePtRuAlloyedRu(min)(nm)a(nm)b(wt.%)c(wt.%)c(%)6–
8.12.11.021125.2±0.35.43.91.224243.4±0.23.66.12.13236
4.2±0.2
4.6
7.2
3.1
26
aMeasuredfromXRDresults.b
MeasuredfromTEMresults.c
MeasuredfromICP-AESresults.
TheloadingmassofthePt–RuwasdeterminedbyInductivelyCoupledPlasma-AtomicEmissionSpectroscopy(ICP-AES)usingaJobinYvonUltima-CSpectrometer.2.4.Electrochemicalmeasurements
Electrochemicalmeasurementswerecarriedoutinaconven-tionalthree-electrodeelectrochemicalcellat25°C.ApieceofPtwirewasusedasthecounterelectrode,andKCl-saturatedAg/AgClwasusedasthereferenceelectrode.Theglassycarbonelectrode,asaworkingelectrode,wascoveredwithcatalystpowder.Allofthesolutionswerepreparedwithultra-purewater.Asolutionof1MCH3OHand0.5MH2SO4wasstirredconstantlyandpurgedwithultra-pureargongas.Electroche-micalexperimentswereperformedusinganAutolabwithaPGSTAT30(EcoChemieB.V.;Netherlands).3.Resultsanddiscussion
3.1.Sizeandloadinglevelofcatalysts
ThecrystallinestructuresofthePt–Ru/CBsandPt–Ru/polyanilinecatalystswereinvestigatedbyX-raydiffraction(XRD).Figs.2and3showtheXRDpatternsofthecatalystspreparedbychangingtheplatingtimeofthestep-potentialplatingmethod.Thepeaksat2θ=40°,47°,68°,and82°wereassociatedwiththe(111),(200),(220),and(311)typesre-spectively.AllofthecatalystsdemonstrateddiffractionpatternssimilartothoseofthePt.ThecharacteristicpeaksforRuwerenotclearlyshownintheXRDpatterns.Inthecaseofthe6minplatingtime,thecharacteristicpeaksofPtwerenotdistinct,indicatinginefficientelectrodepositionofthemetalcatalysts.Forthe12minplatingtime,Pt(111)appearedat~40°.
After
Table2
MeansizeandloadingcontentsofPt–Ru/polyanilinecatalystsPlatingtimeCrystallinesizeParticlesize
PtRuAlloyedRu
(min)(nm)a(nm)b(wt.%)c(wt.%)c
(%)6–
7.42.31.320124.3±0.34.57.63.125242.9±0.23.19.34.63536
3.9±0.3
4.2
11.1
5.3
27
a
MeasuredfromXRDresults.b
MeasuredfromTEMresults.c
MeasuredfromICP-AESresults.
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Fig.4.TEMmicrographofPt–Ru/CBscatalystsby(a)6min,(b)12min,and(c)24minplating
time.
24minplating,thecatalystsshoweddefiniteandenhancedpeakintensityforthefourkindsofpeaks.Inthecaseof36minplating,thecatalystsclearlyshowedthecharacteristicpeaks.ThepreciseloadingcontentsofthecatalystswereobtainedbyusingICP-AESmethods,andaregiveninTable1.TheloadingcontentofPtwasupgradedfrom2.1%to7.2%,andthatofRuwaschangedfrom1.0%to3.1%.Theloadingcontenthadbeenincreasedproportionallyasafunctionofplatingtime.
SimilartotheFig.2results,andasshowninFig.3,thecrystallinepeaksofthepolyaniline-supportedcatalystswerenotclearlyevidentfortheinitialplatingtimeof6min,exceptfortheappearanceofasmallPt(111)peak.After12minplating,thecatalystsshowedthefourcharacteristicpeaks.Within-creasingplatingtimeafter24min,thepeaksbecamesharpanddefinite.
Consideringparticlecrystallinesize,theaveragesizesofCBs-supportedcatalystsshowedthesmallestvalue,3.4nm,at24minplating,asshowninTable1.Beside,particlesizesbyTEMresultswereshowninTables1and2.Inthecaseof6minplatingtime,theaveragesizewas~8nm.Itwasconsideredthatparticlenucleationwasnotasefficientastheparticlegrowthattheinitialstageofelectrodeposition.After24minplating,theparticlenucleationwasefficientenoughtoproduceanew
generationofsmallparticles,resultinginthedecreaseoftheaveragecrystallinesize.AlthoughmoreprecisenucleationandgrowthmechanismsarenecessaryforPt–Runanoparticles,itwasfoundthatthesmallercrystallinesizecouldbeobtainedafteraninitialactivationstate.Thisbehaviorwasalsoobservedinthecaseofpolyanilinesupports,asshowninTable2.Regardlessofthesupportmaterials,thesmallestnanoparticleswereobtainedbyelectrodepositionafter24minplatingtime.TheloadingcontentofPtorRuwas11.1%or5.3%,respec-tively,after36minplatingtime.ThesevalueswereslightlyhigherthatthoseoftheCBssupports.Itwasconcludedthatconductingpolymersupportsaremorebeneficialforahigherloadingforelectrodepositionofcatalysts.
ThepeakpositionofPtRucatalystshadbeenshiftedincomparisonwiththatofpurePtcatalyst.Theshiftofpeakpositioncouldmeanthechangeofalatticeparameter.
Wehadcalculatedthealloyingdegreebythefollowingformula[42];
lPtRu¼0:3916À0:124xRu
ð2Þ
(wherelPtRuisthelatticeparameterofPtRucatalysts,andxRuisthepercentofRuinthealloy).Thelatticparameter
of
Fig.5.TEMmicrographofPt–Ru/polyanilinecatalystsby(a)6min,(b)12min,and(c)24minplatingtime.
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PtRuissmallerthanthatofPt,meaningapartofRuhadenteredintothecrystallatticeofPt.ThealloyingdegreeofRuhadbeeninsertedinTables1and2.
TheparticlesizesandmorphologiesofthePt–Ru/CBsandPt–Ru/polyanilinecatalystswereinvestigatedbyTEM.Fig.4showsaTEMimageofnanoparticlecatalyststhatwerepreparedonCBsbyelectrodepositionwithplatingtime.24minplatingshowedthesmallestparticlesizes.Thisshowsthenanoparticlesinthe2.5–5.0nmsizerange.Fig.5showsaTEMimageofcatalyststhatwerepreparedonpolyanilinesupportswithchangingplatingtime.24minplatingshowsnanoclusterswithindividualparticlesof2.5–4.1nmsize.TheaveragecrystallinesizescalculatedfromtheXRDpeakwidthswerefoundtobefairlyconsistentwiththosefromtheTEMresults,asshowninTables1and2.
3.2.Electrochemicalpropertiesofcatalysts
Theelectrochemicalpropertiesofthecatalystswereinves-tigatedbycyclicvoltammetryin1MCH3OH+0.5MH2SO4aqueoussolution.Fig.6showstherepresentativecurrent–voltagecurvesoftheCBs-supportedcatalysts,presentingtheelectrochemicalbehaviorofmethanoloxidation.VoltammetricbehaviordependsonthePtcontent.Theelectrochemicalactivityincreasedwithincreasingplatingtime,reachingthemaximumat24min,andthenslightlydecreased.However,thecatalystsshowedanincreasedPtcontentwithplatingtimeto36min.Theoptimalplatingtimewas24min,althoughthePtcontentwasthehighestwhentheplatingtimewas36min.Thecatalystby24minplatingshowedthehighestcurrentdensityformethanoloxidation,indicatingthehighestelectroactivitybyanenhancedspecificsurfaceareaofareactionsiteformetalliccatalysts.Thisresultwasconsideredtohavebeenoriginatedfromthecatalyst'ssmallerparticlesizeandloweraggregation.
Inthecaseofthepolyaniline-supportedcatalysts,thecyclicvoltammogramsshowninFig.7alsoexhibitmethanoloxi-dationpeak.ThecatalystdepositedonPANIshowedaratherdefiniteoxidationpeakat~520mV.SimilartotheCBssup-ports,thecatalystsshowedthehighestelectroactivityat24min
Fig.6.CyclicvoltammogramsofPt–Ru/CBscatalystspreparedfordifferentplatingtimesof(a)6,(b)12,(c)24,and(d)36minin1Mmethanolsolution(scanrate:20
mV/s).
Fig.7.CyclicvoltammogramsofPt–Ru/polyanilinecatalystspreparedfordifferentplatingtimesof(a)6,(b)12,(c)24,and(d)36minin1Mmethanolsolution(scanrate:20
mV/s).
plating.Indeed,thecatalystsby24minplatingexhibitedanaveragesizeof3.1nm,whereasthecatalystsby36minplatingshowedanaveragesizeof4.2nm.Smallerparticlesofcatalystsmightresultinalargeavailablecatalystsurfaceareaandgoodelectrocatalyticpropertiesformethanoloxidation.
TodeterminethecarbonandPANIsupportinfluences,in-dividually,ontheoxidationcurrentofcatalysts,supportswith-outmetalcatalystswerestudiedin1MCH3OH+0.5MH2SO4aqueoussolution,asshowninFig.8.Thecarbonsupportdidnotshowanyelectrochemicalactivityexceptforsomesmallcapacitivecurrent.Bycontrast,thePANIsupportshowedadefinitecathodic/anodicpeak,indicatinganoxidation/reductionreaction[38–40].However,itwasconcludedthatpolyanilinesupportscouldnotfunctionaloneascatalystsformethanoloxidation.
Tocheckthespecificsurfaceareaofcatalysts,cyclicvol-tammograms(CVs)hadbeenperformed.Fig.9showstheCVsofthePANI-orCBs-supportedcatalystsin1.0Msulphuricacidsolution.H2adsorption/desorptionpeakwereobservedat 200mVforbothcaseandtheelectrochemicalsurfaceareaarecalculated(PtRu/PANI:4.3cm2,PtRu/CBs:7.4cm2).
By
Fig.8.Cyclicvoltammogramsof(a)CBsand(b)polyanilinesupportsin1Mmethanolsolution(scanrate:20mV/s).
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Fig.9.Cyclicvoltammogramsof(a)Pt–Ru/CBsand(b)Pt–Ru/polyanilinepreparedby24minplatingin1Msulfuricacidsolution(scanrate:20
mV/s).
consideringthedifferentmetalloading,weobtainedthespecificsurfaceareabydividing2themetalweight(PtRu/PANI:62m2/g,PtRu/CBs:75m/g).CatalystdepositedonPANIshowedthehigherspecificsurfaceareathanPtRu/CBs.Thisresultsup-portedthattheeffectivesurfaceareacouldbedependentontheparticlesizeandaggregationdegree.
Beside,chronoamperometrycouldbeusedtoobtaintheap-parentdiffusioncoefficientofionsinelectrochemicalreactions.ThecurrentresponseswithtimewereshowninFig.10.Afterthepotentialwasraisedabruptlyfrom 0.2to0.6V,ingafollowingequation,theapparentdiffusioncoefficienthadbeencalculated[42,43]. lni i¼Àp2Dtð3Þ
Ol
whereioistheinitialcurrent,ithecurrent,lsamplethicknessandtthetime.
Theobtaineddiffusioncoefficientswerelikefollowing;PtRu/PANI:6.1×10 9cm/s,PtRu/CBs:4.2×10 9cm/s.Theformercasewasahighervaluethanthelattercase.Thisresultcouldbeoneofthereasonsoftheimprovedelectroactivity.
Fig.10.Chronoamperometryresultsof(a)Pt–Ru/CBsand(b)Pt–Ru/polyanilineby24minplatingin1Mmethanol
solution.
Fig.11.Specificcurrentdensityforoxidationpeaksof(a)Pt–Ru/CBsand(b)Pt–Ru/polyanilinecatalystspreparedfordifferentplatingtimes((c)CBsand(d)polyanilinesupportsthemselveswereaddedforcomparison)(at600mV).
Fig.11showsthespecificcurrentdensitiesofthepreparedPt–Ru/CBsandPt–Ru/polyanilinecatalysts.Thecurrentden-sitiesofthedifferentmaterials-supportedcatalystsasafunctionofplatingtimeshowedsimilarbehaviours.ThePANI-supportedcatalystsshowedenhancedelectroactivitycomparedwiththecarbon-supportedcatalysts.Intheearlystageof6minplating,thedifferenceofenhancedcurrentdensity(41 9=32(mA/mg))wasalmostsimilartothecurrentdensity(27(mA/mg))ofPANIitself.However,inthecaseof24minplating,thedif-ferenceofincreasedcurrentdensity(121 68=53(mA/mg))wasmuchhigherthanthecurrentdensityofPANIitself.Ac-cordingly,itwasconcludedthattheimprovedelectroactivityofthePANI-supportedcatalystswasaresultnotonlyofthecombinedactivityofthecatalystsandthePANI;oneofthemainsourcesoftheimprovedelectroactivitywasthehighelectronicconductivityofDBSA-dopedpolyaniline(~80S/cm)comparedwiththatoftheCBs(~0.7S/cm)[44].Additionally,wehadfoundthattheelectrochemicalareaofcatalystshadbeenincreased.Theincreasedelectrochemicalareamightberelatedtothesmallparticlesizeandlowdegreeofaggregation.4.Conclusions
Inthepresentstudy,thepreparationandcharacterizationofPt–Ru/CBsandPt–Ru/polyanilinecatalystswereinvestigated.Pt–Ruparticleswere,bystep-potentialplatingmethods,electro-depositedontoCBsandpolyanilinefromdistilledwatersolutioncontainingrutheniumchlorideandchloroplatinicacid.Thepar-ticlesizesofthePt–Rucatalystswereabout3–8nm.Fromtheloadingcontentresultsasafunctionofplatingtime,theefficiencyofloadingwasenhancedtoN11wt.%withtheincreaseoftheplatingtimeto36min.However,fromtheviewpointofaverageparticlesizes,thesmallestnanoparticlesof3.1nmwereobtainedbyelectrodepositionwith24minplatingtime.
Theelectrochemicalactivityincreasedwithincreasingplatingtime,toamaximumof24min,andthendecreased.Theseelec-troactivitychangesasafunctionofplatingtimewereinverselyproportionaltothesizeofthenanoparticlescatalysts,indicatingthatthehigherelectroactivitycouldhavebeenenabledby
the
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decreasingaveragesizeofnanoparticlecatalysts.H2adsorption/desorptionresultsshowedthatPtRu/PANIhadthehigherspecificsurfaceareaforanelectrochemicalreactionthanPtRu/CBs(75N62m2/g).ChronoamperometryresultsindicatedthatPANIsupportsshowedthe9higherapparentiondiffusioncoefficientthanCBs(6.1×10 N4.2×10 9cm/s).Themethanoloxida-tionspecificcurrent(121(mA/mg))forpolyaniline-supportedPt–Rucatalystswashigherthanthat(68(mA/mg))forCBs-supportedPt–Rucatalysts.Theenhancedspecificcurrentdensityofpolyaniline-supportedPt–Runanocompositeswasattributedtotherelativelyhigherelectricalconductivityofthepolyanilineortheincreasedelectrochemicalarea,whichcouldberelatedtothesmallparticlesizeandlowdegreeofaggregation.References
[1]X.Ren,P.Zelenay,S.Thomas,J.Davey,S.Gottesfeld,J.PowerSources
86(2000)111.
[2]C.K.Witham,W.Chun,T.I.Valdez,S.R.Narayanan,Electrochem.Solid-StateLett.3(2003)497.
[3]C.Y.Chen,P.Tang,J.PowerSources123(2002)37.
[4]A.S.Arico,P.Creti,E.Modica,G.Monforte,V.Baglio,V.Antonucci,
Electrochim.Acta45(2000)4319.
[5]A.Lima,C.Cutanceau,J.M.Leger,my,J.Appl.Electrochem.31
(2001)379.
[6]S.Katsuaki,U.Kohei,K.Hideaki,N.Yoshinobu,J.Electroanal.Chem.
256(1988)481.
[7]M.Watanabe,S.Saeguae,P.Stonelhart,J.Electroanal.Chem.271(1989)213.[8]S.Katsuaki,I.Ryuhei,K.Hideaki,J.Electroanal.Chem.284(1990)2523.[9]A.Hamnett,B.J.Kenndey,S.A.Weeks,J.Electroanal.Chem.240(1988)349.[10]M.Gotz,H.Wendt,Electrochim.Acta43(1998)3637.
[11]S.Mukerjee,S.J.Lee,E.A.Ticianelli,J.Mcbreen,B.N.Grgur,N.M.
Markovic,R.N.Ross,J.R.Giallombardo,E.S.Decastro,Electrochem.Solid-StateLett.2(1999)12.
[12]H.A.Gasteiger,N.Markovic,P.N.Ross,E.J.Cairns,J.Phys.Chem.97
(1993)1220.
[13]E.Ticianelli,J.G.Beery,M.T.Paffett,S.Gottesfeld,J.Electroanal.Chem.
258(1989)61.
[14]D.Chu,R.Jiang,SolidStateIonics148(2002)591.
[15]S.Ueda,M.Eguchi,K.Uno,Y.Tsutsumi,N.Ogawa,SolidStateIonics
177(2006)2175.
[16]A.Heinzel,V.M.Barragan,J.PowerSources84(1999)70.[17]J.Cruickshank,K.Scott,J.PowerSources70(1999)70.[18]A.Heinzel,V.M.Barragan,J.PowerSources84(1999)70.
[19]A.Ruffmann,H.Silva,B.Schulte,S.P.Nunes,SolidStateIonics162(2003)269.
[20]T.Frelink,W.Visscher,J.A.Rvan,J.ElectroanalChem.382(1995)65.[21]V.Lordi,J.Yao,J.Wei,Chem.Mater.13(2001)733.
[22]K.H.Choi,H.S.Kim,T.H.Lee,J.PowerSources75(1998)230.
[23]borde,J.M.Leger,my,J.Appl.Electrochem.24(1994)1019.[24]S.K.Ghosh,A.K.Grover,G.K.Dey,A.K.Suri,DefenseSci.J.55(2005)63.[25]C.A.Bessel,ubernds,N.M.Rodriguez,R.T.Baker,J.Phys.Chem.105(2001)1115.
[26]T.Hyeon,S.Han,T.E.Sung,K.W.Park,Y.W.Kim,Angew.Chem.42(2003)4357.
[27]A.S.Arico,A.K.Shulka,K.M.Khatib,P.Creti,V.Antonucci,J.Appl.Electrochem.29(1999)671.
[28]S.Kim,S.J.Park,J.PowerSources159(2006)42.
[29]S.Kim,M.H.Cho,J.R.Lee,S.J.Park,J.PowerSources159(2006)46.[30]S.Kim,S.J.Park,Electrochim.Acta52(2007)3013.
[31]W.Li,C.Liang,J.Qiu,W.Zhou,J.Qiu,Z.Zhou,G.Sun,Q.Xin,J.Phys.Chem.B107(2003)6292.
[32]B.Rajesh,T.K.Ravindranathan,J.M.Bonard,B.Viswanathan,J.Mater.Chem.10(2000)1757.
[33]E.S.Steigerwalt,G.A.Deluga,D.E.Cliffel,C.M.Lukehart,J.Phys.Chem.B105(2001)8097.
[34]S.H.Joo,S.J.Choi,I.Oh,J.Kwak,Z.Liu,O.Terasaki,R.Ryoo,Nature412(2001)169.
[35]J.H.Choi,K.Y.Park,Y.M.Kim,J.S.Lee,Y.E.Sung,Electrochim.Acta48(2003)2781.
[36]i,P.D.Beattie,F.P.Orfino,E.Simon,S.Holdcroft,Electrochim.Acta44(1999)2559.
[37]K.M.Kost,D.E.Bartak,B.Kazee,T.Kuwana,Anal.Chem.60(1988)2379.[38]S.Kim,I.J.Chung,SyntheticMetals97(1998)127.
[39]A.G.MacDiarmid,A.J.Epstein,FaradayDiscuss.Chem.Soc.85(1989)317.[40]A.N.Aleshin,K.Lee,J.Y.Lee,D.Y.Kim,C.Y.Kim,SyntheticMetals99(1999)27.
[41]K.Kinoshita,Carbon:ElectrochemicalandPhysicochemicalProperties,JohnWiley,NewYork,1988,p.31.
[42]E.Antoline,F.Cardellini,J.AlloysCompd.315(2001)118.
[43]A.J.Bard,L.R.Faulkner,ElectrochemicalMethod,Wiley,NewYork,1980Chapter.3,6,and10.
[44]S.Kim,I.J.Chung,SyntheticMetals96(1998)213.
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