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TuningcatalyticperformancesofcobaltcatalystsforH2production
viavariationofthetypeofcarbonsupport
HuiZhang1*,Y.AAhamld2,FeiHuang1,L.A.Petrov2
1SchoolofChemistryandChemicalEngineering,SouthwestPetroleumUniversity,Chengdu610500,;
2SABICChairofCatalysis,KingAbdulazizUniversity,Jeddah21589,SA
hui
:Ammonia position;H2production;Cobaltcatalysts;Carbonsupports
Hydrogen,asapotenialrenewablecleanenergy,hasbeenattractingmoreandmoreattentioninrecentyears[1].Liquidammonia,asahydrogencarrier,hastheadvantagesofbothhighenergydensityandhighhydrogenstoragecapacity(17.7%),whiakesammoniasuitableforon-boardgenerationofCOxhydrogenbycatalyticammonia position[2].Thedevelopmentofhighlyactive,stableandcheapsolidcatalysttobenifitammonia positionatlowtemperatureisstillachanllagingissuetodate.Anidealcatalystsupportforammonia positionshouldpossesshighelectronicconductivity,thermalstabilityandsurfacearea[2,3].NovelcarbonmaterialsexceptactivatedcarbonssuchasMulti-wallcarbonnanotubes,singlewallcarbonnanotubeandreducedgrapheneoxides,havebeenwidelyemployedascatalytcarriersduetotheirexcellentmechanicalstabilityandspecialelectrinicpropeties.
Severalcarbonmaterialsupportswereobtainedassupport:(1)Muti-wallcarbonnanotubes( Ts);(2)activecarbonwithdifferenttexturalstructure,AC-1,AC-2andAC-3;(3)Singlewallcarbonnanotubes, Ts;(4)reducedgrapheneoxides,RGO.Theserialofcarbonmaterials-supportedcobaltcatalysts(5wt%)wereprepared,labeledlike Ts,Co/AC-1,Co/AC-2,Co/AC-3, TsandCo/RGO,respectively.ThesampleswerecharacterizedusingXPS,N2-TPD,TEM,XRDandH2-TPRtechniques.Theammonia positionto
hydrogenreactionwascarriedoutinafixed-bedreactoratatmosphericpressure.
Table1.Texturalpropertiesofcarbonmaterials
Surfacearea Totalporevolume Averageporediameter
Carbonsupport
m2.g-1 cm3.g-1
nm
Ts
169.3
0.41
9.7
AC-1
2954.0
1.56
2.1
AC-2
695.2
0.41
2.1
AC-3
71.3
0.08
4.5
*OpenFundofStateKeyLaboratoryofOilandGasReservoirGeologyandExploitation,SouthwestPetroleumUniversityof(PLN1132);KingAbudulazizUniversityofSaudiArabia(ProjectHiCi-1432/4-4).
Table1reportsthephysicalcharacteristicsofthesupportmaterials.ItisapparentthatthreetypesofAChaveverydifferenttexturalcharacteristics.ThesurfaceareaandporevolumeofAC-1are2954m2g-1and1.6cm3g-1,respectively,whicharemuchlargerthanthesamevaluesoftheothertwotypesofACsupports.TheAC-3hasthesmallestsurfaceareaandporevolumeof71.3m2g-1and0.08cm3g-1,respectively,whileitsaverageporediameterof4.51nmwasthelargestamongthethreetypesofusedAC.Thesurfacearea,porevolumeandaverageporediameterofTssupportwas169.3m2/g,0.41cm3/gand9.7nm,respectively.Theorderofdecreasing
surfaceareaofACand TsusedascatalystsupportwasAC-1>AC-2> Ts>AC-3.
Fig.1.CatalyticactivitiesofCocatalystsforNH3 positionatdifferentreactiontemperatures
(A)andGHSV(B).
Fig.1showstheeffectofreactiontemperature(Fig.1(A))andNH3GHSV(Fig.1(B))onammoniaconversionondifferentcatalysts.FromFig.1(A)follows,thatNH3conversionwasreasedwithreasingofthereactiontemperature,suggestingthathighreactiontemperatureisfavorableforammonia positionreaction.Onthecontrary,ammoniaconversiondecreasedwiththe reaseofNH3GHSV,butthisdependencewasnotverystrong(seeFig.1(B)).Thus,theeffectofreactiontemperatureoncatalyticperformancewasgreaterthantheeffectofNH3GHSV
forammonia position.
CombiningthedatainFig.1(A)and(B),itfollowsthatregardlessofthereactiontemperatureandGHSV, TscatalysthasshownthehighestNH3conversion.Thecatalyticactivitiesofthepreparedcatalystswererankedinthefollowingorder: Ts>Co/AC-1>Co/AC-2>Co/AC-3>Co/RGO> Ts.
AhighlyefficientCocatalystforCOx-H2productionviaNH3 positionshouldhavethecombiningpropertiesofelectronictransportpropertiesandappropriatecarbonsupportstructure.
Acknowledgement.HuiZhangthankstheSABICChairofCatalysisforprovidingfinancialsupportduringhisstayinSaudiArabiaforexperimentresearch.
References
C.M.White,R.R
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