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当前位置:首页 > 行业资料 > 冶金工业 > 硅源对蒸氨法制备CuSiO2催化剂催化甲醇裂解制氢的影响杜泽宇
Received2018-01-26Revised2018-04-20.*Correspondingauthor.Tel18205182971E-mailmingzhu84@njtech.edu.cn.Cu/SiO2112!1111121.2100092.210009Cu/SiO2SiO2-aer、SiO2-gelSiO2-solCu/SiO2N2-、N2O、ICP-AES、XXRD、H2H2-TPR、TEMXXPS。Cu/SiO2。Cu/SiO2-sol。280℃1MPa0.6h-1Cu/SiO2-aerCu/SiO2-gelCu/SiO2-sol10%7%CH4CO298.4%96.7%。Cu/SiO2O643.88ACatalyticperformanceofmethanoldecompositiononCu/SiO2catalystwithdifferentsilicasourcespreparedwithammoniaevaporationmethodDUZe-yu1ZHUMing12*BAOZhe-yu1SHIDa-you1CHENXiao-rong1XUYan1MEIHua121.CollegeofChemistryandChemicalEngineeringNanjingUniversityofTechnologyNanjing210009China2.CatalyticHydrogenationEngineeringTechnologyResearchCenterNuomengChemNanjing210009ChinaAbstractCu/SiO2catalystswerepreparedviaammoniaevaporationmethodusingfumedsilicaSiO2-aersilicagelSiO2-gelandalkalinesilicasolSiO2-solasthesilicasourcesandtheircatalyticperformanceinmethanoldecompositionwereinvestigated.ThecatalystswerecharacterizedbyN2adsorption-desorptionN2OchemisorptioninductivelycoupledplasmaatomicemissionspectroscopyICP-AESX-raydiffractionXRDH2temperatureprogrammedreductionH2-TPRtransmissionelectronmicroscopeTEMandX-rayphotoelectronspectroscopyXPS.TheresultsindicatethatsilicasourcecanaffectthedecompositionactivityofCu/SiO2catalysts.TheCu/SiO2-solcatalystpreparedwithalkalinesilicasolexhibitslargersurfaceareasmalleractivesitesizeandmoreuniformdispersionofCu.ThereforeitgivesCu/SiO2-solabetterdecompositionperformancethanothercatalysts.MethanolconversiononCu/SiO2-solis10%higherthanthatonCu/SiO2-aerand7%higherthanthatonCu/SiO2-gel.AdditionallybyproductsconcentrationonCu/SiO2-solisconsiderablylowerthanothercatalysts.Underthereactionconditionsof280℃1MPaand0.6h-1ofWHSVmethanolconversionof98.4%andgasyieldof96.7%canbeachieved.KeywordsmethanoldecompositionammoniaevaporationmethodCu/SiO2catalyst、。1-3。4-6。78。9、1011。Pd。12PdO-HCOsHs。Wang13Ni111。CH4CO2。Greeley1446620186JournalofFuelChemistryandTechnologyVol.46No.6Jun.2018Cu111。。Cu/SiO2。15Cu/SiO216Cu/SiO2。Ji17Cu/SiO2。、Cu/SiO2CuO181920。Cu/SiO22122Cu/SiO2Cu/SiO2。11.1。。。30%。。1.2Cu/SiO2。CuNO32·3H2OSiO230%。Cu2+0.5mol/LNH3·H2OpH11.0-12.0。0.03g/g。25℃4h90℃。pH7.0-8.0。90℃12h450℃4h。Cu/SiO236%。Cu/SiO2Cu/SiO2-aerCu/SiO2-gelCu/SiO2-sol。1.3AnkersmidBELSORPIIN2BET。200℃3h。N2OTPR。100mg200℃Ar2h60℃10%H2-Ar20mL/min5℃/min360℃S1。Ar60℃N2O30minAr30min10%H2-Ar20mL/min5℃/min360℃S22S2/S1。CuNa+OPTMA20000VICP-AES。50mg500mL。XRDBrukerD8AdvanceXCuKα40kV40mA10°-80°20°/min。H2-TPRTPR100mg200℃Ar2h10%H2-Ar20mL/min5℃/min400℃TCD。JEOLJEM-200CX。。ThermoESCALAB250XIX。1.4Cu/SiO2100cm25mm7.9g。150mL/min250℃6h。280℃6mL/h。3966Cu/SiO21MPa280℃1MPa0.6h-1。xwx=min-moutmin×100%1w=VoutVideal×100%2Videal=3minVmM3min、moutVoutVidealMVm。GC-97905Aφ3.0mm×1m100℃100℃100℃80mATCD。GC-2014XE-60135℃135℃FID。22.11。1Dong23Cu/SiO2。Cu/SiO2-aerCu/SiO2-gelCu/SiO2-sol、。。Na+ICP-AES。Cu/SiO236%Cu/SiO2-sol。Na+。1Cu/SiO2Table1TexturalpropertiesoftheCu/SiO2catalystspreparedwithdifferentsilicasourcesCatalystBETaA/m2·g-1Porevolumeav/cm3·g-1Averageporeadiameterd/nmCudispersionb/%Contentw/%cCuNaSiO2-aer359.20.8311.11---SiO2-gel324.90.9610.27---SiO2-sol192.80.24.12---Cu/SiO2-aer512.80.473.3520.133.2B.D.Cu/SiO2-gel555.30.422.7122.333.7B.D.Cu/SiO2-sol580.60.694.0924.834.5B.D.adeterminedbyN2adsorption-desorptionbdetectedbyN2OchemisorptioncdeterminedbyinductivelycoupledplasmaatomicemissionspectroscopyICP-AESB.D.=belowdetection2.2XRD1Cu/SiO2XRD。122.0°SiO2。31.2°、35.8°、57.2°63.1°24。Cu/SiO2-gelCu/SiO2-aerCu/SiO2-sol。25450℃CuOCuOH2CuO。1CuOCuO26XRD。2Cu/SiO2250℃XRD。243.2°、50.4°74.5°Cu0。Cu02Cu/SiO2-solCu0Cu/SiO2-aerCu/SiO2-gelCu0Cu/SiO2-aerCu/SiO2-gelCu/SiO2-solCu0。496461Cu/SiO2XRDFigure1XRDpatternsoftheCu/SiO2catalystspreparedwithdifferentsilicasourcesaCu/SiO2-aerbCu/SiO2-gelcCu/SiO2-sol2Cu/SiO2XRDFigure2XRDpatternsofthereducedCu/SiO2catalystspreparedwithdifferentsilicasourcesaCu/SiO2-aerbCu/SiO2-gelcCu/SiO2-sol2.3H2-TPR3Cu/SiO2H2-TPR。3Cu/SiO2。CuOCu0Cu+CuOLi27。Cu/SiO2-aerCu/SiO2-gel230221℃Cu/SiO2-sol216℃。Cu/SiO2-gelCu/SiO2-aerCu/SiO2-sol。3Cu/SiO2H2-TPRFigure3H2-TPRprofilesoftheCu/SiO2catalystspreparedwithdifferentsilicasourcesaCu/SiO2-aerbCu/SiO2-gelcCu/SiO2-sol2.4TEM4Cu/SiO2TEM。4Cu/SiO2-aerCu/SiO2-gelCu/SiO2-aerCuO。Cu/SiO2-solCuOCu/SiO2-solCu/SiO2-sol。4Cu/SiO2Figure4TEMimagesoftheCu/SiO2catalystspreparedwithdifferentsilicasourcesaCu/SiO2-aerbCu/SiO2-gelcCu/SiO2-sol5Cu/SiO2250℃TEM。5Cu/SiO2-aerCu/SiO2-gelCu/SiO2-sol2。5966Cu/SiO25Cu/SiO2Figure5TEMimagesofthereducedCu/SiO2catalystspreparedwithdifferentsilicasourcesaCu/SiO2-aerbCu/SiO2-gelcCu/SiO2-sol2.5XPS6Cu/SiO2XPS。6Cu/SiO2XPSFigure6XPSspectraoftheCu/SiO2catalystsaftercalcinationsaCu/SiO2-aerbCu/SiO2-gelcCu/SiO2-sol6Cu2p3/2935-936eV943eVCu+228。Yu29Cu/SiO2。Cu/SiO2Cu2p3/2Cu/SiO2-aerCu/SiO2-gelCu/SiO2-sol935.9eV。2.6Cu/SiO2280℃1MPa0.6h-12。2Cu/SiO2-aer88.7%86.1%Cu/SiO2-gel91.7%89.5%。Cu/SiO2-aerCu/SiO2-gelCu/SiO2-sol98.4%96.7%。2Cu/SiO2Table2CatalyticperformanceoftheCu/SiO2catalystswithdifferentsilicasourcesinmethanoldecompositionCatalystMethanolconversionx/%Gasyieldw/%Concentrationφ/%CH4CO2Cu/SiO2-aer88.786.11.042.12Cu/SiO2-gel91.789.50.81.93Cu
本文标题:硅源对蒸氨法制备CuSiO2催化剂催化甲醇裂解制氢的影响杜泽宇
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