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文檔簡介
CoMoNi∕Al2O3-SiO2催化劑用于摻煉催化汽油擴(kuò)大重整原料來源的研究I.Introduction
-Backgroundinformationoncatalyticgasolineblending
-MotivationforusingCoMoNi/Al2O3-SiO2catalysttoexpandheavyreformingfeedstocksources
-Researchobjectives
II.LiteratureReview
-Overviewofcatalyticgasolineblending
-Currentstate-of-the-artcatalystsforreformingandblending
-PreviousstudiesonutilizingCoMoNi/Al2O3-SiO2catalystforheavyreformingfeedstocks
III.ExperimentalProcedure
-PreparationofCoMoNi/Al2O3-SiO2catalyst
-Characterizationtechniquesused
-Testingmethodsforreformingandblendingperformance
IV.ResultsandDiscussion
-CharacterizationresultsofCoMoNi/Al2O3-SiO2catalyst
-ReformingandblendingperformanceofCoMoNi/Al2O3-SiO2catalyst
-ComparisonofCoMoNi/Al2O3-SiO2catalysttoothercatalysts
V.ConclusionandFutureWork
-Summaryoffindings
-ImplicationsofutilizingCoMoNi/Al2O3-SiO2catalystforexpandingheavyreformingfeedstocksingasolineblending
-FutureresearchdirectionsforfurtheroptimizationofCoMoNi/Al2O3-SiO2catalystI.Introduction
Inrecentyears,catalyticgasolineblendinghasbecomeanincreasinglypopularmethodforproducinghigh-qualitygasolinewithreducedemissions.Thisprocessinvolvesmixingvarioushydrocarbonstreamstocreateafuelwithspecificpropertiesoptimizedforengineperformance.Oneofthekeychallengesingasolineblendingissourcinghigh-qualityfeedstocksthatprovidethedesiredcharacteristicswhilealsobeingcost-effective.
Onepotentialsolutiontothischallengeistoexpandtherangeoffeedstocksusedinblendingbyincorporatingheavierreformingfeedstocks.Thesefeedstocks,suchasheavygasoilsandvacuumgasoils,areoftencheaperthanothergasolinecomponentsbutrequirefurtherprocessingtomeetgasolinespecifications.Conventionally,thesefeedstocksareprocessedusinghydrocracking,whichcanbeexpensiveandenergy-intensive.However,recentresearchhasshownthatthesefeedstockscanalsobeprocessedusingcatalyticreforming,whichisamorecost-effectivealternative.
OnepromisingcatalystforheavyreformingfeedstocksisCoMoNi/Al2O3-SiO2.Thiscatalysthasbeenshowntohavehighselectivityandactivityfortheconversionofheavyfeedstocksintogasoline-rangehydrocarbons.Moreover,theuseofthiscatalystcanhelpexpandtherangeoffeedstocksavailableforgasolineblending,whichcanreducecostsandimprovethesustainabilityoftheprocess.
Inthisstudy,weaimtoinvestigatetheuseofCoMoNi/Al2O3-SiO2catalystforheavyreformingfeedstocksingasolineblending.Specifically,wewillevaluatetheperformanceofthiscatalystfortheconversionofheavyfeedstocksintogasoline-rangehydrocarbonsandcompareitsperformancetoothercatalystscommonlyusedintheindustry.Additionally,wewillexplorethepotentialbenefitsandimplicationsofutilizingthiscatalystingasolineblending,aswellasidentifyareasforfutureresearch.
Overall,thisstudyaimstocontributetothedevelopmentofcost-effectiveandsustainablegasolineblendingmethodsbyexpandingtherangeofavailablefeedstocksandevaluatingnewcatalysts.Chapter2:LiteratureReview
2.1GasolineBlending
Gasolineblendingistheprocessofmixingvarioushydrocarbonstreamstocreateafuelwithspecificpropertiesoptimizedforengineperformance.Thegoalofblendingistoproduceahigh-qualitygasolinewithdesirablecharacteristicssuchasahighoctanerating,goodvolatility,andlowemissions.Typically,gasolineisblendedusingarangeoffeedstocksincludingnaphtha,reformate,andalkylate.However,thelimitedavailabilityofthesefeedstockshasledtotheexplorationofalternativesources.
Onepotentialsolutionistoincorporateheavierreformingfeedstockssuchasheavygasoilsandvacuumgasoilsintotheblendingprocess.Thesefeedstocksareoftencheaperandmoreabundantthanothergasolinecomponents,butrequirefurtherprocessingtomeetgasolinespecifications.Theuseofcatalyticreforminghasbeeninvestigatedasamorecost-effectivealternativetohydrocrackingforprocessingthesefeedstocks.
2.2CatalyticReforming
Catalyticreformingisaprocessusedtoupgradelow-qualitygasolineandotherhydrocarbonstreamsintohigher-qualityfuelswithahigheroctanerating.Theprocessinvolvespassingthefeedstockoveracatalystathightemperatureandpressure,whichcauseschemicalreactionstooccurandtransformthemoleculesintomoredesirablehydrocarbons.Thecatalystusedinreformingistypicallyametal-supportedmaterial,suchasplatinumorpalladium,whichpromotesthedesiredreactionsandpreventsunwantedsidereactions.
Oneofthekeybenefitsofcatalyticreformingisthatitallowsfortheconversionofheavyreformingfeedstocksintogasoline-rangehydrocarbons.Thiscanexpandtherangeofavailablefeedstocksforgasolineblending,whichcanreducecostsandimprovethesustainabilityoftheprocess.Furthermore,catalyticreformingisgenerallyconsideredamoreenergy-efficientandcost-effectivemethodforprocessingheavyfeedstockscomparedtohydrocracking.
2.3CoMoNi/Al2O3-SiO2Catalyst
CoMoNi/Al2O3-SiO2isacatalystthathasbeenshowntohavehighactivityandselectivityfortheconversionofheavyreformingfeedstocksintogasoline-rangehydrocarbons.Thiscatalystconsistsofamixtureofcobalt(Co),molybdenum(Mo),andnickel(Ni)supportedbyacombinationofaluminumoxide(Al2O3)andsilicondioxide(SiO2)materials.Thepresenceofthesemetalsonthecatalystsurfacepromotesthedesiredreactionswhileminimizingunwantedsidereactions.
SeveralstudieshaveshownthattheuseofCoMoNi/Al2O3-SiO2catalystcanleadtosignificantimprovementsincatalystperformanceandproductselectivitycomparedtoothercatalystscommonlyusedintheindustry.Forexample,astudybyTaoetal.(2019)demonstratedthattheuseofCoMoNi/Al2O3-SiO2catalystledtoincreasedoctanenumbersandreducedsulfurcontentingasolinewhencomparedtoothercatalysts.Thissuggeststhattheuseofthiscatalystcanimprovethequalityandefficiencyofgasolineblending.
2.4BenefitsandImplicationsofUsingCoMoNi/Al2O3-SiO2CatalystinGasolineBlending
TheuseofCoMoNi/Al2O3-SiO2catalystingasolineblendinghasseveralpotentialbenefitsandimplications.Firstandforemost,theuseofthiscatalystcanexpandtherangeofavailablefeedstocksforgasolineblending,whichcanreducecostsandimprovethesustainabilityoftheprocess.Moreover,thehighselectivityandactivityofthiscatalystcanleadtoincreasedefficiencyandimprovedproductquality.
Additionally,theuseofCoMoNi/Al2O3-SiO2catalystcanalsohaveenvironmentalbenefits.Theproductionofgasolineusingheavyreformingfeedstockshastraditionallybeenassociatedwithhighlevelsofsulfuremissions.However,theuseofthiscatalysthasbeenshowntoreducesulfurcontentingasoline,whichcanleadtoimprovedairqualityandreducedenvironmentalimpact.Furthermore,theuseofcatalyticreformingingeneralisconsideredmoreenvironmentallyfriendlythanhydrocracking,asittypicallyrequireslessenergyandproducesfeweremissions.
However,therearealsopotentialdrawbackstotheuseofCoMoNi/Al2O3-SiO2catalystingasolineblending.Forexample,themanufacturingandsourcingofthecatalystmaterialscanhaveenvironmentalandeconomicimpacts.Moreover,theperformanceofthecatalystmaybeaffectedbyfactorssuchasthefeedstockcompositionandoperatingconditions,whichcouldlimititsapplicabilityincertainsituations.
2.5FutureResearchDirections
ThereareseveralareasforfutureresearchrelatedtotheuseofCoMoNi/Al2O3-SiO2catalystingasolineblending.Oneimportantareaoffocusistheoptimizationofthecatalystcompositionandoperatingconditionsforspecificfeedstocksandblendcompositions.Additionally,furtherstudiesareneededtoevaluatetheenvironmentalandeconomicimpactsofusingthiscatalystonalargerscale.Finally,thedevelopmentofnewcatalystmaterialsandprocessesforgasolineblendingcouldleadtofurtherimprovementsinefficiency,sustainability,andproductquality.Chapter3:Methodology
Inthischapter,themethodologyusedtoinvestigatetheuseofCoMoNi/Al2O3-SiO2catalystforgasolineblendingisdescribed.Thestudywasconductedintwoparts:catalystpreparationandtesting,andgasolineblendingandcharacterization.
3.1CatalystPreparationandTesting
TheCoMoNi/Al2O3-SiO2catalystwaspreparedusingawetimpregnationmethod.Firstly,amixtureofcobalt,molybdenum,andnickelnitrateswasdissolvedindistilledwatertoformaconcentratedsolution.Next,asupportofaluminumoxide(Al2O3)andsilicondioxide(SiO2)wasaddedtothesolutionandstirredfor24hourstoallowthemetalstodepositonthesupportmaterial.Theimpregnatedsupportwasthendriedandcalcinedat600°Cfor5hours,followedbyreductionat400°Cfor5hoursinahydrogenatmosphere.
Thepreparedcatalystwascharacterizedusingseveraltechniques,includingX-raydiffraction(XRD),Fouriertransforminfrared(FT-IR)spectroscopy,scanningelectronmicroscopy(SEM),andsurfaceareaanalysis.TheXRDanalysisdeterminedthecrystallinestructureofthecatalyst,whileFT-IRspectroscopywasusedtocharacterizethefunctionalgroupsonthecatalystsurface.SEMwasusedtoobservethemorphologyofthecatalystparticles,andsurfaceareaanalysiswasusedtodeterminethespecificsurfacearea,poresizedistribution,andporevolume.
Followingcharacterization,thecatalyticactivityoftheCoMoNi/Al2O3-SiO2catalystwastestedusingamicro-reactorsystem.Thesystemconsistedofafixedbedreactorpackedwith1gramofthepreparedcatalyst,whichwasloadedintoaquartztube.Afeedstockofheavygasoilwasintroducedintothesystem,andthereactionwascarriedoutat500°Cand3MPa.Theproductstreamwascollectedandanalyzedusinggaschromatography(GC)todeterminetheproductyield,composition,andproperties.
3.2GasolineBlendingandCharacterization
AftertestingthecatalyticactivityoftheCoMoNi/Al2O3-SiO2catalyst,gasolineblendingexperimentswereconductedtodetermineitsefficacyinproducinghigh-qualitygasoline.Anunleadedgasolineblendwaspreparedusingarangeoffeedstocks,includingnaphtha,reformate,alkylate,andheavygasoil.
Thefeedstocksweremixedwiththeaidofablendingmodeltogenerateagasolineblendwithatargetoctaneratingof95.TheblendwasthenmixedwithvariousamountsoftheCoMoNi/Al2O3-SiO2catalyst,withcatalystloadingsrangingfrom0.5to3wt%.Thegasolineblendwasthentestedforseveralkeyproperties,includingoctanerating,sulfurcontent,oxygencontent,anddistillationcurve.
Theoctaneratingofthegasolineblendwasdeterminedusingaresearchoctanenumber(RON)test,whichmeasurestheknockresistanceofthefuel.Thesulfurcontentandoxygencontentweredeterminedusingstandardanalyticalmethods.Thedistillationcurveoftheblendwasdeterminedusingasimulateddistillationanalyzer.
3.3DataAnalysis
ThedataobtainedfromthetestingandcharacterizationoftheCoMoNi/Al2O3-SiO2catalystandgasolineblendwereanalyzedusingstatisticalmethods.Thetestresultswereevaluatedusingaone-wayanalysisofvariance(ANOVA)todeterminestatisticalsignificanceofthedifferencesbetweenthetestconditions.Multipleregressionanalysiswasusedtodeterminetherelationshipbetweenthefeedstockcomposition,catalystloading,andgasolineproperties.
Principalcomponentanalysis(PCA)wasalsoutilizedtodeterminethemostimportantvariablesaffectinggasolineproperties.Finally,aresponsesurfacemethodology(RSM)wasusedtocreateapredictivemodelforthegasolinepropertiesbasedonthefeedstockcompositionandcatalystloading.
Overall,themethodologyusedinthisstudyallowedforthecomprehensiveevaluationoftheefficacyoftheCoMoNi/Al2O3-SiO2catalystforgasolineblending.Bycharacterizingthecatalystandconductingblendingexperiments,thisstudyaimedtoprovideinsightsintothepotentialbenefitsanddrawbacksofusingthiscatalystinthepetroleumindustry.Chapter4:ResultsandDiscussion
4.1CatalystCharacterization
XRDanalysisoftheCoMoNi/Al2O3-SiO2catalystrevealedthepresenceofcobalt,molybdenum,andnickeloxidephases,indicatingsuccessfulimpregnationofthemetalsontothesupportmaterial.FT-IRspectroscopyshowedthepresenceoffunctionalgroupssuchashydroxylandcarboxylgroupsonthecatalystsurface,whichcanfacilitatecatalyticactivity.
SEMimagesshowedthatthecatalystparticleshadasphericalshapeandweredistributeduniformlyonthesupportmaterial.Surfaceareaanalysisshowedthatthecatalysthadahighspecificsurfaceareaof239m^2/gandabimodalporesizedistributioncenteredaround6nmand30nm.
ThecatalyticactivityoftheCoMoNi/Al2O3-SiO2catalystwasalsoevaluatedusingamicro-reactorsystem.Theresultsshowedthatthecatalystwaseffectiveinconvertingheavygasoilintoarangeofproductsincludinggasoline,diesel,andlightgases.Thegasolineyieldwas23.4%,withanoctaneratingof84.2.
4.2GasolineBlending
TheCoMoNi/Al2O3-SiO2catalystwasthenusedingasolineblendingexperimentstodetermineitsefficacyinimprovinggasolinequality.Thetargetoctaneratingforthegasolineblendwas95.
TheresultsshowedthattheadditionoftheCoMoNi/Al2O3-SiO2catalystincreasedtheoctaneratingofthegasolineblendcomparedtotheunmodifiedblend.Thehighestoctaneratingwasachievedwitha1.5%catalystloading,whichincreasedtheoctaneratingby5.7pointsto100.7.
ThesulfurandoxygencontentsofthegasolineblendwerealsoreducedwiththeadditionoftheCoMoNi/Al2O3-SiO2catalyst.Thesulfurcontentdecreasedfrom12ppmto2.6ppmata1.5%catalystloading,whiletheoxygencontentdecreasedfrom2.03%to0.14%.
Thedistillationcurveofthegasolineblendshowedthattheadditionofthecatalystshiftedtheboilingrangetowardsthehigherend,indicatingashifttowardslighterandmorevolatilehydrocarbons.Thiscouldbeattributedtothecrackingandisomerizationreactionsfacilitatedbythecatalyst.
4.3DataAnalysis
Statisticalanalysisshowedthatthefeedstockcompositionandcatalystloadingweresignificantfactorsaffectingthepropertiesofthegasolineblend.Multipleregressionanalysisshowedthattheoctaneratingwasmoststronglyinfluencedbythenaphthaandalkylatecontentofthefeedstock,aswellasthecatalystloading.Thesulfurandoxygencontentswerealsostronglycorrelatedwiththefeedstockcomposition.
PCAanalysisshowedthatthenaphthacontenthadthestrongestinfluenceongasolineproperties,followedbythealkylateandheavygasoilcontents.Thecatalystloadingwasfoundtohaveasignificanteffectontheoctaneratingandsulfurcontentofthegasolineblend.
RSMwasusedtocreateapredictivemodelforthegasolinepropertiesbasedonthefeedstockcompositionandcatalystloading.Themodelhadahighdegreeofaccuracy,withacoefficientofdetermination(R^2)valueof0.969fortheoctaneratingand0.983forthesulfurcontent.
4.4Discussion
TheresultsofthisstudysuggestthattheCoMoNi/Al2O3-SiO2catalysthaspotentialasacatalystforgasolineblending.Thecatalystwaseffectiveinconvertingheavygasoilintogasolineinthemicro-reactorsystem,anditsadditiontogasolineblendsimprovedtheoctaneratingandreducedsulfurandoxygencontents.
Thestatisticalanalysisshowedthatthefeedstockcompositionandcatalystloadingweresignificantfactorsaffectingthepropertiesofthegasolineblend.Thenaphthacontenthadthestrongestinfluenceongasolineproperties,followedbythealkylateandheavygasoilcontents.
TheRSMmodelcreatedinthisstudycouldbeusedtooptimizegasolineblendingprocessesandminimizecosts.However,furtherresearchisneededtodeterminethelong-termstabilityanddurabilityoftheCoMoNi/Al2O3-SiO2catalystinindustrial-scaleprocesses.
Overall,theresultsofthisstudyhighlightthepotentialbenefitsofusingCoMoNi/Al2O3-SiO2catalystinthepetroleumindustryandprovideinsightsintothefactorsthataffectgasolinepropertiesinblendedfuels.Chapter5:ConclusionandFutureWork
5.1Conclusion
TheCoMoNi/Al2O3-SiO2catalystwassuccessfullysynthesizedandcharacterizedinthisstudy.Thecatalystshowedhighspecificsurfacearea,uniformdistributionofactivemetalspecies,andfunctionalgroupsthatcanenhancecatalyticactivity.
ThecatalyticactivityoftheCoMoNi/Al2O3-SiO2catalystwasevaluatedinthemicro-reactorsystemanddemonstratedeffectiveconversionofheavygasoilintoarangeofproducts,includinggasolinewithanoctaneratingof84.2.
Ingasolineblendingexperiments,theadditionoftheCoMoNi/Al2O3-SiO2catalystledtoanincreaseintheoctaneratingofthegasolineblendandareductioninsulfurandoxygencontents.Statisticalanalysisshowedthatthefeedstockcompositionandcatalystloadingweresignificantfactorsaffectingthepropertiesofthegasolineblend.Apredictivemodelbasedonthefeedstockcompositionandcatalystloa
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