Synthesis of high performance hydroxyapatite-gold catalysts for CO ...

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Tim White is currently Associate Professor at the School of Materials Science and Engineering and Director of the Facility for Advanced Characterisation, Testing ...
3YNTHESISOF(IGH 0ERFORMANCE (YDROXYAPATITE 'OLD #ATALYSTSFOR #//XIDATION .OPPHAWAN0HONTHAMMACHAI A :HONG:IYI B'UO*UN A(AN9I&AN B AND4*7HITEA A

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!BSTRACT #ATALYSTSFORLOWTEMPERATURE#/OXIDATIONWERE PREPAREDBYDECORATINGHYDROXYAPATITE(!P CERAMIC FOAMSCAFFOLDSWITHHIGHLYDISPERSEDGOLD NANOCRYSTALSUSINGADEPOSITION PRECIPITATION$0 PROCESS#ATALYTICACTIVITY MICROSTRUCTUREAND CRYSTALLINITYWERESTUDIEDASAFUNCTIONOFREAGENT P(  ANDAGINGTIME  MIN FORPOWDERS ANDPOROUSSUPPORTS3UPERIORPRODUCTSWITHSMALL ‘NM GOLDCRYSTALSDISTRIBUTEDHOMOGENEOUSLYOVER (!PFOAMWEREOBTAINEDATP( ,ARGERCRYSTAL SIZESANDCOLLOIDALGOLDAGGLOMERATIONAPPEAREDAT LONGERAGINGTIMES4HEOPTIMIZEDCATALYSTPREPARED BYREACTIONATP(FORMINSHOWED#/ CONVERSIONTO#/AT€#4HE!U (!PCOMPOSITE DEMONSTRATEDEXCELLENTDURABILITYBYRETAINING STRUCTURALANDCRYSTALLOGRAPHICINTEGRITYWITHNOLOSS OFACTIVITYWHENTESTEDAT€#OUTTOH

+EYWORDS #/OXIDATION DEPOSITION PRECIPITATIONPROCESS GOLD NANOCRYSTAL HYDROXYAPATITE

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)NTRODUCTION 4HE CATALYTIC ACTIVITY OF OXIDE SUPPORTED GOLD NANOPARTICLES HAS BEEN EXPLOITED IN MANY APPLICATIONS INCLUDING CHEMICAL SENSING HYDROGENPRODUCTION FUELCELLS ANDVARIOUSCHEMICAL PROCESSES;=OFWHICHCARBONMONOXIDEOXIDATIONISTHEBEST KNOWN;=3EVERALMECHANISMSHAVEBEENPROPOSEDTOEXPLAIN THE ENHANCED ACTIVITY AT THE METAL OXIDE INTERFACE INCLUDING THEPRESENCEOFHIGHLYREACTIVESURFACEGOLDATOMSATGROWTH STEPS;= THEEASEOFCHARGETRANSFERATTHEBOUNDARY;= AND IN THE CASE OF REDUCIBLE SUPPORTS THE PROVISION OF ACTIVATED OXYGENTHATCANBETRAPPEDATREACTIONSITES;=7HATEVERTHE MEANS ITISEVIDENTTHATINTERACTIONSBETWEENTHESUPPORTAND THE GOLD MUST BE TAILORED FOR PERFORMANCE ENHANCEMENT 7HILEPOROUSBINARYOXIDESSUCHASALUMINA;=ORZIRCONIA;= ARE FREQUENTLY USED AS CATALYTIC SCAFFOLDS THE SEARCH FOR SUPPORTS WHOSE PROPERTIES WILL AMPLIFY THE REACTIVITY OF NANOSIZEDGOLDCONTINUES/NESUCHMATERIALISHYDROXYAPATITE (!P WHOSE POTENTIAL AS A COMPONENT OF ENVIRONMENTALLY BENIGN CATALYSTS HAS NOT BEEN WIDELY CONSIDERED ALTHOUGH PHOTOCATALYTIC MINERALISATION OF POLLUTANTS ;= AND OXIDATIVE DECOMPOSITION OF METHANOL ;= HYDROCARBON ;= TRICHLOROBENZENE AND CHLOROETHYLENE ; = HAVE BEEN DEMONSTRATED0ROGRESSINTHIS½ELDHASBEENHAMPEREDPARTLY BECAUSE (!P IS CRYSTALLOCHEMICALLY COMPLEX ;= AND ALSO BECAUSE IT HAS BEEN DIF½CULT TO PREPARE WITH POROUS ARCHITECTURES ALTHOUGHMETHODSTOCONSTRUCTINVERSEOPALINE STRUCTURES; =ANDFOAMS; =ARENOWAVAILABLE)NDEED APATITICCHEMISTRYISDIVERSEWITHSOMEANALOGUESINTRINSICALLY CATALYTIC; = ANDTHESEFORMSMAYINTERACTFAVORABLYWITH METALLICCO CATALYSTSSUCHASGOLDTOINVIGORATEREACTIVITY $EPOSITION PRECIPITATION $0 IS A RELIABLE METHOD TO PREPARE OXIDE SUPPORTED GOLD ; = IN WHICH THE KEY PARAMETERISTHEISOELECTRICPOINT)%0 OFTHESCAFFOLDMATERIAL -OREAU ET AL ;= FOUND THAT THE DEPOSITION RATE OF AGGLOMERATEDGOLDCRYSTALSONTITANIAACCELERATEDWITHP( )%0ASTHEPOSITIVESURFACECHARGEATLOWERP(ATTRACTEDGOLD BEARING ANIONS !U#L  (OWEVER WITH P(  )%0 THE TITANIA SURFACE CARRIED A NET NEGATIVE CHARGE AND ELECTROSTATIC REPULSIONOFANIONSRESULTEDINHIGHLYDISPERSEDGOLDCRYSTALS WITHTHECOVERAGEIN¾UENCEDBYMANYFACTORSINCLUDINGTHE CONCENTRATIONOF(!U#L THEVOLUMETOMASSRATIOOF(!U#L TOSUPPORT THEBASETYPE.A/( .(/( UREA AGINGTIME AND TEMPERATURE PROCESSING STEPS ½LTRATION WASHING AND DRYINGSTEPS ANDCALCINATIONTEMPERATURE;=3ELECTIONOF THE ALKALINE SOLUTION PROVES ESPECIALLY CRITICAL IN CONTROLLING THEYIELD DISPERSIONANDSIZEOFGOLDCRYSTALS&OREXAMPLE :ANELLAETAL;=FOUNDTHATDURING$0IN.A/(THEGOLDWAS PARTIALLY REDUCED TO METAL AFTER DRYING AT €# BUT A COMPARABLE EXPERIMENT IN UREA DELAYED METALLIZATION TO CALCINATIONTEMPERATURES€# 7HILE $0 SYNTHESES OF GOLD NANOPARTICLES ON REDUCIBLE 4I/ &E/ #O/ ; =ANDNON REDUCIBLEOXIDES3I/ !L/ ; =HAVEBEENWIDELYREPORTEDANDTHECATALYTIC MECHANISMSINVESTIGATED CORRESPONDINGEXAMINATIONOF(!P SUPPORTS ARE SPARSE 4HE NOTABLE EXCEPTION IS THE STUDY OF



6EMUGOPALETAL;=WHERE!UAND2U DEPOSITEDFROM (!U#LX(/ AND 2U#L(/ AT P(  FOR H PRODUCED A CATALYSTUSEDTOPROMOTEALOWTEMPERATUREWATER GASSHIFT REACTION)TWASFOUNDTHAT!U(!PSHOWEDTHEHIGHERACTIVITY WITHCONVERSIONTO#/AND(ACHIEVEDAT€# BUT CORRELATIONOFPREPARATIVECONDITIONSWITHRESPECTTOTHESIZE DISPERSIONANDCATALYTICACTIVITYOFTHEGOLDCRYSTALSREQUIRES CLARI½CATION 4HIS REPORT DESCRIBES A $0 METHOD THAT HOMOGENEOUSLYDISTRIBUTESGOLDNANOCRYSTALSNMAVERAGE DIAMETER OVER POROUS (!P TO CREATE A HIGHLY EF½CIENT AND DURABLECATALYSTFOR#/OXIDATION4ECHNIQUESTOCONTROLTHE SIZEANDDISPERSIONOFMETALLICCRYSTALSON(!PAREDETAILED PARTICULARLYWITHRESPECTTOTHEMANNEROFSUPPORTSYNTHESIS P(CONTROLANDAGINGTIME

%XPERIMENTAL (YDROXYAPATITE(!P SUPPORTFABRICATION (!P WAS SYNTHESIZED BY MIXING  G CALCIUM NITRATE #A./   -ERCK AND  G .( (0/  !LDRICH IN  ML .(/( -ERCK AND  ML DOUBLY DEIONIZEDWATER4HESUSPENSIONWASHEATEDTO€#WITH MAGNETIC STIRRING FOR  MIN AFTER WHICH THE TEMPERATURE WASRAISEDTO€#ANDSTIRRINGCONTINUEDFORMIN4HE PRECIPITATED(!PWASSEPARATEDUSINGVACUUM½LTRATIONAND WASHED SEVERAL TIMES PRIOR TO OVEN DRYING OVERNIGHT AT €# #RYSTALLIZATION WAS PROMOTED BY DEWATERING AT €# WITH A HEATING RATE OF €# MIN  FOR  MIN FOLLOWEDBYSOAKINGAT€#FORHRWITHAHEATINGRATE OF€#MIN  4HE (!P FOAM SUPPORT WAS PREPARED IN A TWO STAGE PROCESS;=&IRST METHYLCELLULOSEC0SVISCOSITY !LFA !ESAR WASDISSOLVEDINMLOFDEIONIZEDWATERTHENAERATED WITHASTAINLESSSTEELBLADEAGITATORAT RPMFORMIN 3ECOND A SUSPENSION OF  ML (/ AND  G (!P WAS ADDEDTOTHEPOLYMERSOLUTIONWITHAGGRESSIVEMIXINGFOR MIN4HEPOLYMERFOAMIMPREGNATEDWITH(!PWASCALCINED AT€#€#MIN  FORMINTOREMOVEORGANICSPRIORTO ½NALSINTERINGFORHRS€#€#MIN   'OLDDEPOSITION PRECIPITATION$0 'OLDSTOCKSOLUTIONSWEREPREPAREDBYADDING-.A/( 3IGMA !LDRICH DROPWISE TO  ML OF  M- (!U#L (!U#L(/ !LFA !ESAR UNTIL THE P( STABILIZED AT PREDETERMINEDVALUESRANGINGFROMTO(!PG WAS DISPERSED IN THE SOLUTION WHICH WAS AGED AT €# WITH VIGOROUS STIRRING FOR  MIN AFTER WHICH THE GOLD LOADED CATALYSTSWERECOLLECTEDBY½LTRATIONANDWASHEDREPEATEDLY WITH DEIONIZED WATER TO REMOVE CHLORIDE 4HE POWDER WAS OVEN DRIED OVERNIGHT AT €# PRIOR TO AIR CALCINATION AT €#€#MIN  FORH -ATERIALSCHARACTERIZATION 4HE CRYSTALLOGRAPHIC PARAMETERS AND PHASE CONTENT OF THE (!P SUPPORT AND GOLD LOADED CATALYSTS WERE DETERMINED

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FROMPOWDER8 RAYDIFFRACTION82$ PATTERNS3HIMADZU,!" 82$  COLLECTEDATK7USING#U+αRADIATION3PECIMENS WEREPREPAREDFORDIFFRACTIONBYPACKINGPOWDERINTOAGLASS HOLDER × CM WITH INTENSITY COLLECTED BY STEP SCANNING OVERTHEθRANGE€TO€ININCREMENTSOF€ANDA DWELL TIME OF  S 2IETVELD ANALYSIS AS IMPLEMENTED IN 4/0!3; =WASUSEDFORQUANTITATIVEPHASEDETERMINATION WITH HYDROXY¾UORAPATITE ;= AND GOLD ;= EMPLOYED AS CRYSTALLOGRAPHIC MODELS IN A SIMULATION THAT INCLUDED A BACKGROUND POLYNOMIAL SCALE FACTOR CELL PARAMETERS PREFERREDORIENTATIONANDZEROPOINTCORRECTION)NTHISWAY POWDER82$WASUSEDTODETERMINEPHASECONTENT CONDUCT MASSBALANCEANDESTIMATECRYSTALSIZE#ATALYSTMORPHOLOGY WAS EXAMINED USING A ½ELD EMISSION SCANNING ELECTRON MICROSCOPE3%- *%- OPERATEDINSECONDARYELECTRON IMAGING3%) MODEATK64OAVOIDCHARGING THEPOWDERS WERE PRESSED INTO A CARBON TAPE ATTACHED TO AN ALUMINUM STUB FOLLOWED BY GOLD COATING USING A LOW ENERGY PLASMA -ICROGRAPHS OF THE PYROLYZED SAMPLES WERE OBTAINED AT MAGNI½CATIONSOF× AND× "RIGHT½ELDTRANSMISSION ELECTRONMICROSCOPY4%- *%-& WASCONDUCTEDAT K6.ITROGENADSORPTION DESORPTIONISOTHERMSWEREUSEDTO DETERMINE SURFACE AREA AND POROSITY -ICROMERITICS !3!0  VIATHE"RUNAUER %MMETT 4ELLER"%4 METHOD!MIXED GAS OF NITROGEN AND HELIUM WAS ALLOWED TO ¾OW THROUGH THE ANALYZER AT A CONSTANT RATE OF  CCMIN .ITROGEN WAS USED TO CALIBRATE THE ANALYZER AND ALSO SERVED AS THE ADSORBATEATLIQUIDNITROGENTEMPERATURE4HESAMPLESWERE THOROUGHLYOUTGASSEDFORHAT›#BEFOREEXPOSURETOTHE ADSORBENTGAS #ATALYTICTESTING #ATALYTIC OXIDATION OF #/ WAS CONDUCTED IN A ½XED BED MICROREACTORUSINGACATALYSTCHARGEOFMG0RIORTOTESTING THE MATERIAL WAS HEATED IN AIR AT €# FOR  H TO REMOVE IMPURITIES!FTERCOOLINGTOROOMTEMPERATURE AREACTANTGAS CONTAININGVOL#/INAIRWASPASSEDTHROUGHTHECATALYST BEDWITHAGASHOURLYSPACEVELOCITY'(36 OFH 4HE OUTLETGASESWEREANALYZEDBYANON LINEGASCHROMATOGRAPH '# 3HIMADZU " EQUIPPED WITH THERMAL CONDUCTIVITY 4#$ AND¾AMEIONIZATION&)$ DETECTORS#ATALYSTDURABILITY WASESTABLISHEDBY½XINGTHETEMPERATUREOFTHEREACTORAT €# FOR  H UNDER THE SAME FEED CONDITIONS USING THE !U (!PMATERIALPREPAREDATP(

2ESULTSAND$ISCUSSION 3TRUCTUREOF(!PSUPPORT "OTHTHEDRIEDANDCALCINEDPOWDERSCONTAINEDSINGLEPHASE (!P AS DETERMINED BY POWDER 8 RAY DIFFRACTION &IGURE  WITHTHEAVERAGECRYSTALLITESIZEINCREASINGFROMTONM AFTER HEAT TREATMENT 4ABLE   -ATCHING OF SIMULATED AND EXPERIMENTALDIFFRACTEDPATTERNSINVARIABLYREQUIREDCORRECTION OFL RE¾ECTIONINTENSITIESTHATWEREENHANCEDASARESULT OFACICULARFACETING3UBSEQUENTINCORPORATIONOF(!PINTHE



4ABLE 0HYSICALPROPERTIESOFDRIED CALCINEDANDFOAM(!PSUPPORTS

3AMPLE

"%4 0ORESIZE (!P SURFACEAREA NM CRYSTALSIZE

NM MG 

$RIED(!P







#ALCINED(!P







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DETERMINEDBY82$ 800

CERAMIC FOAM AND ½RING AT €# DID NOT PERCEPTIBLY CHANGE THE CRYSTALLINITY OR TEXTURE 4ABLE   4HE CALCINED POWDERCONTAINEDLARGEAGGREGATES ”M OF(!PCRYSTALS WHILETHECERAMICFOAMCONSISTEDOFSPONGYMACROPOREWALLS OFHIGHPOROSITY&IGURE  4HEHIGHESTSURFACEAREAWITHTHELARGESTPORESIZE NM ASDETERMINEDBYTHE"%4PROCEDUREWASOBTAINEDFROM DRIED (!P BUT DECREASED DRAMATICALLY AFTER CALCINATION AT €#DUETOCRYSTALGROWTH4ABLE 0RIORTOCALCINATION THEDRIED(!PPOWDERSHOWEDATYPE)6NITROGENADSORPTION DESORPTIONISOTHERM&IGUREA WITHAHYSTERESISLOOPOFTYPE ( CONSISTENT WITH SLIT PORE MESOPOROSITY ; = !FTER

(a)

Hydroxyapatite 100.00%

600

Counts

400

200

0

-200

10

20

30

40

50

60

70

80

2Th Degrees 2,500 (b)

Hydroxyapatite 100.00%

2,000

Counts

1,500 1,000 500 0 -500

10

20

30

40

50

60

70

80

2Th Degrees &IGURE 2IETVELDPLOTSOF82$PATTERNSOFA POWDER(!PANDB FOAM(!PCALCINEDAT€#4HEEXPERIMENTALINTENSITYISSHOWNASCIRCLESANDTHESIMULATED PATTERNASASOLIDLINE4HEINTENSITYDIFFERENCEBETWEENTHESEPATTERNSISSHOWNBELOW4HE"RAGGDIFFRACTIONMARKERSFOR(!PARESHOWNATTHEBOTTOM OFEACHPLOT

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4ABLE #ORRELATION OF (!P SUPPORT AND DEPOSITION PRECIPITATION CONDITIONS ON GOLDCRYSTALSIZEANDLOADING

(!P

P( !GINGTIME !ULOADING !UCRYSTALSIZE MIN NM

0OWDER 







&OAM









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DETERMINEDBY82$ CALCINATION THE POWDER AND FOAM GAVE TYPE )) ISOTHERMS &IGUREB ASTHEMESOPORESCOLLAPSEDLEADINGTOUNRESTRICTED MONOLAYER MULTILAYER ADSORPTION ;= 4HIS CON½RMS THAT WHILE THE CERAMIC FOAM IS MACROPOROUS ITS PORE WALLS ARE COMPOSED OF DENSE (!P PARTICLES RATHER THAN MESOPOROUSMATERIAL

%FFECTOF(!PSUPPORTON#/OXIDATION 'OLD NANOCRYSTALS DEPOSITED ON CERAMIC FOAM (!P WERE GENERALLYEVENLYDISTRIBUTED ANDOFSMALLERANDMOREREGULAR SIZE THANTHOSE½XEDTOTHEPOWDER4ABLE &IGURE 4HE !U LOADEDFOAMWASALWAYSMOREACTIVEWITHTHEOPTIMIZED MATERIAL ACHIEVING  #/ CONVERSION AT €# A TEMPERATURE €# LOWER THAN THE ANALOGOUS CALCINED POWDER&IGURE !STHEAPATITEFOAMWITHOUTGOLDWASNOT CATALYTIC IT IS CLEAR THAT THE SIZE AND DISPERSION OF GOLD PARTICLESCONTROL#/OXIDATIONACTIVITY 4HEPRECISEFUNCTIONOFTHE(!PSUPPORTDURINGCATALYSIS WILLREQUIRECLARI½CATION BUTRECENTSTUDIESOFGOLDNANOCRYSTALS LOADEDONPHOSPHATE DOPEDTITANIA ORATTACHEDTOMONOCLINIC ANDHEXAGONAL,A0/ SUGGESTTHEPHOSPHATEGROUPSSTABILIZE !U CRYSTALS PREVENTING THEIR AGGLOMERATION AND ENHANCING #/CONVERSIONATHIGHTEMPERATURES; =4HEFUNCTIONOF THECRYSTALSTRUCTURESUPPORTISSUBTLE ASINTHECASEOF,A0/ GREATER#/CONVERSIONWASACHIEVEDONLYWITHCATALYSTSUSING THEHEXAGONALDIMORPH4HESERESULTSAREINACCORDWITHTHE PRESENT INVESTIGATION WHERE THE SIZE OF THE GOLD CRYSTALS DECORATING (!P REMAINED CONSTANT AFTER CALCINATION TO €#(OWEVER THEMECHANISMOF#/CONVERSIONMUSTBE DISTINCT DUETOTHEDIFFERENTCHEMISTRY CRYSTALSTRUCTUREAND OXYGEN TRANSFERENCE EF½CIENCY OF APATITE !S (!P IS BOTH

300 Quantity adsorbed (cm3 g-1)

(a)

(a)

250 200 150 100 50 0 0.0

(b)

Quantity adsorbed (cm3 g-1)

6

0.2

0.4 0.6 0.8 Relative pressure (P/P0)

1.0

0.2

0.4 0.6 0.8 Relative pressure (P/P0)

1.0

(b)

5 4 3 2 1 0 0.0

&IGURE &IGURE 3%)MICROGRAPHSOFCALCINEDA POWDER(!PANDB FOAM(!P

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.ITROGENADSORPTION DESORPTIONISOTHERMSOFA DRIEDANDB CALCINED FOAM(!P



(a)

(a)

100 nm

(b)

20 nm

(b)

100 nm

(c)

20 nm

&IGURE "RIGHT½ELD4%-IMAGESOFGOLDDECORATINGA CALCINEDPOWDERANDB FOAM(!PSYNTHESIZEDATP(ANDANAGINGTIMEOFMIN

140

Au-powder HAp, pH8, 60 min, 0.1% Au (14 nm) Au-foam HAp, pH8, 60 min, 4.8% Au (8 nm) Calcined foam HAp

120 %CO Conversion

100 nm

(d)

100 80 60 40 20 0 0

50

100 150 200 250 Temperature (°C)

300

100 nm

350

&IGURE

&IGURE

#OMPARISONOFTHE#/CONVERSIONEF½CIENCYOFCALCINEDFOAM(!P GOLD LOADEDCALCINEDPOWDERANDFOAM(!P

(!PLOADEDGOLDNANOCRYSTALGROWTHANDDISPERSIONATP(A  B  C ANDD AGINGTIMEMIN

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Separated colloidal gold cluster

20 nm

100 nm

&IGURE

&IGURE

4%-IMAGEOFANHEDRALGOLDNANOCRYSTALSP(

,ARGECOLLOIDALGOLDCLUSTERFORMATIONP( AGINGTIMEMIN

POLYMORPHICANDZEOLITIC;=WITHAWIDERANGEOFCHEMICAL ANALOGUES A SYSTEMATIC STUDY OF CRYSTALLOCHEMICAL VARIANTS EG IRON ZINC OR MAGNESIUM REPLACEMENT OF CALCIUM AND PHOSPHOROUS MAYPRODUCESUPERIORCATALYTICSUPPORTS

;!U#L/( = ISPREVALENT DEPOSITINGONMANYNUCLEATIONSITES THATLEADSTOGOLDCRYSTALSOFSMALLERSIZEANDHIGHERDISPERSION 7HEN THE P( INCREASES TO  WHICH EXCEEDS THE )%0 GOLD DEPOSITIONISIMPEDEDBYELECTROSTATICREPULSIONBETWEENTHE (!PSURFACEANDGOLDHYDROXIDECOMPLEXES4HEGEOMETRICAL CON½GURATIONOFTHEGOLDNANOCRYSTALSCONTROLSTHENUMBER OFCO ORDINATIVELYUNSATURATEDSITES3PHERICALTOPOLOGYWAS DOMINANT &IGURE  AND PROVIDES HIGHER SELECTIVITY AND TURNOVER FREQUENCY 4/& ; = COMPARED TO FACETED OR MULTIPLY TWINNEDPARTICLES-40S  1UANTITATIVE 8 RAY DIFFRACTION CLEARLY SHOWS THE P( DEPENDENCEOFGOLDLOADINGANDCRYSTALLINITY4ABLE &IGURE  &ROMP( THEGOLDLOADINGINCREASESBYMORETHANAN ORDER OF MAGNITUDE BUT DECLINES AT HIGHER P( 4HE GOLD CRYSTAL SIZE DETERMINED FROM THE 82$ PEAK WIDTH IS CHARACTERISTICALLYSLIGHTLYSMALLERTHANDIRECTOBSERVATIONSBY 4%- ASEACHPARTICLEISCOMPOSEDOFCRYSTALDOMAINMOSAICS

%FFECTOFP(ON#/OXIDATIONACTIVITIES 4HEDISTRIBUTIONANDSIZEOFGOLDNANOCRYSTALSWASCONTROLLED BY ADJUSTING THE P( FROM  TO  TO INCREASE HYDROLYSIS OF

;!U#L= TO;!U/( = ANDREDUCETHEADSORPTIONOFCHLORIDE &IGURE  4ABLE   7HILE NEUTRAL !U#L(/ IS THE PRINCIPLE SPECIESATP( ^ ;   =HYDROXYCHLORIDEANIONS

!U#LX/( X OCCUR FROM MID P( UNTIL AT P(  !U/(  IS DOMINANT4HEREFORE INACIDICCONDITIONSADSORPTIONOFGOLD COMPLEXESON(!PSURFACESTAKESPLACESLOWLYANDISOFLIMITED

EXTENT !T P(  AND  THE CONCENTRATION OF ;!U#LX/(  X= INCREASESASDOESTHENUCLEATIONANDGROWTHOFGOLD!TP(   WHICH SPANS THE )%0 OF (!P AROUND  ;= ANIONIC

5000

120 2θ = 38.2°, Au (111)

3000

f e d c b a

2000 1000 0 20

40 60 2θ (Degree)

80

%CO Conversion

4000 Count

pH6, 60 min, 1.5% Au (8 nm) pH8, 60 min, 4.8% Au (8 nm) pH9, 60 min, 2.4% Au (5 nm) pH12, 60 min, 0.8% Au (6 nm)

140

100 80 60 40 20 0 0

50

100 150 200 250 Temperature (°C)

300

&IGURE

&IGURE

82$PATTERNSOFA THEPUREFOAM(!PANDAFTERGOLDDEPOSITIONATP(S B  C  D  E ANDF AGINGTIMEMIN

#ORRELATIONOFP(WITH#/CONVERSIONOFGOLDLOADED CALCINED FOAM(!P

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350



pH8, 60 min, 4.8% Au (8 nm) pH8, 10 min, 3.1% Au (8 nm)

100 %CO Conversion

Reaction rate (mmol CO/gAu/s) x 10-3

120

80 60 40 20 0 0

3.0 pH9, 60 min, 2.4%Au (5 nm)

2.5 2.0 1.5 1.0 0.5 0.0

20 40 60 80 100 120 140 160 180 200 Temperature (°C)

0

20

40

60 80 100 120 140 160 180 Reaction time (h)

&IGURE

&IGURE

#ORRELATIONOF!UCRYSTALGROWTHTIMEWITH#/CONVERSIONEF½CIENCYOF (!PLOADEDGOLD

#/CONVERSIONOF!U LOADED(!PATP(ASAFUNCTIONOFREACTIONTIME AT€#

)N ADDITION THE LARGE GOLD CLUSTERS THAT APPEAR AT P(  INDEPENDENT OF THE (!P SUPPORT ARE ONLY RECOGNIZED BY MICROSCOPY&IGURE  #OMPLETE#/CONVERSIONWASOBTAINEDAT^€#FORTHE CATALYSTSPREPAREDATP(AND&IGURE WITHTHELATTER PROVINGMARGINALLYSUPERIOR ASTHEGOLDCRYSTALSWERESLIGHTLY SMALLER  NM VERSUS  NM  4HE LEAST #/ CONVERSION WAS OBSERVED FOR P(  MATERIAL WHICH HAD THE LARGEST GOLD SIZENM WITHLEASTDISPERSIONASEVIDENTFROM4%-IMAGES &IGURE 

REACTIONRATEWITH#/CONVERSIONATATEMPERATUREOF €#&IGURE 

%FFECTOFGOLDPARTICLESIZEON#/OXIDATIONACTIVITY &ORTHEOPTIMALP(CATALYSTS THE$0AGINGTIMEWASVARIED FROM ANDMINTOSYSTEMATICALLYADJUSTCRYSTALSIZE 4HE SMALLEST UNIFORM !U SIZE  NM WAS OBTAINED AT THE SHORTESTAGINGTIMEMIN 4HISMATERIALGAVETHEFASTEST

$URABILITY 4HE DURABILITY AND STABILITY OF !U LOADED (!P AT P(  WAS TESTEDBYMAINTAININGTHETEMPERATUREOFTHEREACTORAT€# FOR  H &IGURE   4HE #/ OXIDATION ACTIVITY REMAINS CONSTANT AS A FUNCTION OF REACTION TIME UNLIKE METAL OXIDE SUPPORTED !U CATALYSTS SUCH AS #U-N/ ;= AND 4I/ ; =WHEREDEACTIVATIONOCCURREDRAPIDLYDUETOGROWTHOFTHE !UCRYSTALS; =4HISISASIGNI½CANTPROBLEMFORNANOGOLD CATALYSTSTHATMAKESTHEMUNSUITABLEFORLONGTERMUSEHAS BEENOVERCOMEUSINGTHE(!PSCAFFOLD&ROMTHE4%-IMAGE OFTHECATALYSTAFTERTHEDURABILITYTEST&IGURE ITISEVIDENT THATTHEAVERAGESIZEANDDISPERSIONOF!UPARTICLESHASNOT CHANGED4HEREASONFORTHEENHANCEDSTABILITYOFNANOGOLD ON(!PREMAINSTOBEINVESTIGATED

#ONCLUSIONS

100 nm

&IGURE "RIGHT½ELD4%-IMAGESHOWINGTHATTHESMALLSIZEANDHIGHDISPERSION OF!UNANOCRYSTALSISMAINTAINEDAFTERTHEDURABILITYTESTWASCONDUCTED AT€#FORH

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#ATALYSTS COMPOSED OF HIGHLY DISPERSED GOLD NANOCRYSTALS ON A MACROPOROUS (!P FOAM WERE PREPARED USING A $0 METHODFROMA.A/(BUFFEREDSOLUTIONOFGOLDCHLORIDE4HE PHASE PURE (!P WAS SYNTHESIZED AS CALCINED POWDER AND CERAMICFOAMWITHCRYSTALSIZESOFANDNMRESPECTIVELY !LTHOUGH THE SURFACE AREAS WERE EQUIVALENT THE FOAM FAVOUREDTHEDEPOSITIONOFANHEDRALGOLDCRYSTALSOFSMALLER SIZE AND HIGHER DISPERSION TO CREATE EFFECTIVE CATALYSTS 4HE P( OF THE (!U#L SOLUTION CONTROLS THE SPECIATION OF !U#LX/(  XANIONSWHICHATTENUATESTHERATESOFDEPOSITION SUCH THAT SMALLER CRYSTALS ‘  NM AND HOMOGENEOUS DISTRIBUTIONS WERE OBTAINED FROM P(   NEAR THE )%0 OF (!P,ONGERREACTIONTIMESRESULTEDINLARGERCRYSTALSIZESAND COLLOIDALGOLDCLUSTERSSEPARATEDFROMTHE(!P&ORSAMPLES PREPARED AT P(   WITH AN AGING TIME OF  MIN  CONVERSION OF #/ TO #/ AT THE LOW REACTION TEMPERATURE €# WAS ACHIEVED /VER A TEST PERIOD OF  H AND AREACTIONTEMPERATUREOF€#THECATALYSTSHOWEDSTRUCTURAL



AND CRYSTALLOGRAPHIC STABILITY WITHOUT MEASURABLE LOSS OFACTIVITY

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