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2009374200937420093742009374200937420093742009374200937420093742009374FCC、、。70%FCC。FCC。。FCC。[1]。210×104t/aVGO、CGO、DAO。FRIPPFF-14FZC。15~20%w、0.2%w[2]。11.12006630FF-14。。2006630200676。FZC-103A∶3t、FZC-103∶5.6t、FZC-204∶11.20tFF-14∶148.8t。1.271613:45DMDS1000kg。7175:30H2SH2S0.3%。、。27.6101%89%。1.320067212006816181970-1992。210×104t/aVGO、CGO、DAO,。。。TheIndustrialApplicationofWaxOilHydrotreatingandCatalyticCrackingCombinedProcessZHOUYing-qianSinopecGuangzhouBranch,GuangdongGuangzhou510726,ChinaAbstract:GuangzhouPetrochemical210×104t/awaxoilhydrogenationwasoneoftheprojectoftheMiddleEastsourcrudeoilprocessingandproductionofcleanfuels.Usinghydrotreatingconversiontechnologies,VGO,CGO,DAOthroughhydrotreating,inordertoprovidehigh-qualitygasoilcatalyticcrackingunitofrawmaterials.Thewaxoilhydrotreatingandcatalyticcrackingcombinedprocess,notonlyincreasdthesulfurcontentofcrudeoilcapacity,butasloimprovedtheproductdistributionandreducedoperatingcosts,increasdeconomicefficiency,whichplayedanimportantrole.Theeffectofthehydro-treatingandthecombinedprocesswereanalyzedthatwasfocusedoninthepaper.Keywords:hydrotreating;combinedprocess;industrialapplication510726178··20093742009374200937420093742009374200937420093742009374200937420093749.0MPa、400∶1、1.5h-1335℃786μg/g。335℃370℃35℃9.0MPa1.0MPa786μg/g、190μg/g、66μg/g。2200/、100/。VGO、CGOVGO、、DAO。CGO、DAOBVGOVGO。2006721。。200660.6%81.3~1.5%0.92g/cm30.905g/cm30.98%0.15%0.4%0.2%350℃13%2%0.65%0.4%0.01%0.007%。2006620068、FCC200668。、、42.4648.95%、12.12%14.89%、2.923%、4.13%2.484%、1.56%。5647。33.1、、、、FCCFCCFCC。10、、、、。200/12.98、5.54。3.2200757/。210817。70/20[3]817×57/-210×70/-817×20/=1.551.55/。3.3182CGOVGODAO12FCCC/%2.9232.484/%12.1214.89/%42.4648.95/%33.7528.49/%76.2177.44/%4.131.56/%4.263.31/%0.350.31/41.87MJ/t55.9547.0721FCC、7/m%/m%/m%/m%/m%2006060.574~0.6890.661~0.9140.616~0.7070.061~0.0950.062006070.695~0.8360.66~0.1510.717~1.050.034~0.0810.072006081.325~1.540.16~0.460.167~0.4520.006~0.010.032006091.055~1.3170.167~0.550.221~0.3890.009~0.0010.031.81.410.60.20315642716151413121110980.40.81.21.6179··20093742009374200937420093742009374200937420093742009374200937420093744.3Na2SO4Na2SO4Na2SO4CaOH2。51pH、Na+。2pH=8.2~9、=2.5~3、[Na+]=0.15mol/L3600mg/Nm390%。3。4Ca∶S=1.152min。SO2。[1],,,.、.:,2008.[2],..:,2007.[2],..:,2007.[3],,..:,2006.[4],.-.:,2006.[5],..:,2006.[6],,..,2001,215:534-537.[7]..:.2006.[8]DL/T5196-2004,.4=3pH[Na+]=0.2mol/L[Na+]=0.15mol/L[Na+]=0.1mol/L[Na+]=0.05mol/L100908070605040302010066.577.588.28.58.79/%pH179、60.6%81.4%0.08%0.03%。70%、。3.4DAOVGO、DAODAO。3.5SOx、NOx。2006721SO21000mg/Nm335mg/Nm3545mg/Nm3362mg/Nm3。41FCC。2、、。3FF-14。4VGOCGOVGODAOVGOCGO、DAOFF-14。5、、。[1].FFHT.,2008,37:15-20.[2].FCCFF-14.,20083738-43.[3]1.8Mt.,20022320-22.!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!182··
本文标题:蜡油加氢和催化裂化组合工艺的应用
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