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:2015-5-13:(1961-),,,,.:.376:1674-2869(2015)06-0001-04J.WuhanInst.Tech.Vol.37No.6Jun.2015201560、、、(),.,,,.:[1]、[2]、-[3]、[4]、[5]、[6]、[7-9]、[10].-、、.,1#,,.,2#.11.1DF-101S,;,;HN101,;,;DL-1,;50mL,.1.2:,,42.54%,34.38%,23.08%.:1#、2#、1#2#.1.3,,.,250mL,,.,、、,,,.1.4:,GB/T260—1977;:,SY/T0530—1993;:η=m1m×100%m1,m.22.11#,89.9%,32.57%.沈喜洲1,2,王道楠2,尹先清1,段金庭3,谢圣龙2,祝进成2,张保沙21.长江大学化学与环境工程学院,湖北荆州434020;2.武汉工程大学化工与制药学院,湖北武汉430074;3.中国石油天然气股份有限公司大港分公司,天津300280:,,2#.1#,.、,.,:60g,1#6g,1#0.6g,2#6g,2#0.5g.,15.74%,83.52%,0.74%,95.05%.:;;;:TE992.3:Adoi:10.3969/j.issn.1674-2869.2015.06.00137,,.,1#、2#、1#2#,,2#.2.1.1脱水剂1#的用量1#0.6g、2#6g、2#0.608g,1#.30g,2∶160g,60℃、30min、1000r/min,1#、1、2.1、2,1#,,1#6g,1#,;,;1#6g.,1#6g.2.1.2脱泥剂1#的用量1#6g、2#6g、2#0.608g,1#.30g,2∶160g,60℃、30min、1000r/min,1#、3、4:3、4,1#,,1#0.6g;,1#,,,,11#Fig.1Effectsofthedosageofthedehydratingagent1#onthesolidcontentsandwatercontentsofrecoveredoil246810121#/g0.900.800.700.600.50/%45403530252015/%31#Fig.3Effectsofthedosageofthedeslimingagent1#onthesolidcontentsandwatercontentsofrecoveredoil0.00.81.62.41#/g0.950.850.750.650.55/%363228242016/%41#Fig.4Effectsofthedosageofthedeslimingagent1#onrecoveryrateoftreatedsludge0.00.51.01.52.02.51#/g95.094.093.092.091.090.0/%21#Fig.2Effectsofthedosageofthedehydratingagent1#onrecoveryrateoftreatedsludge246810121#/g94.594.093.593.092.592.091.591.0/%26;,1#0.6g.,1#0.6g.2.1.3脱泥剂2#的用量1#6g、1#0.6g、2#0.608g,2#.30g,2∶160g,60℃、30min、1000r/min,2#、5、6.5、6,2#,,2#6g;,2#6g,2#,,,,;6g.,2#6g.2.1.4脱水剂2#的用量1#6g、1#0.6g、2#6g,2#.30g,2∶160g,60℃、30min、1000r/min,2#、7、8.7、8,2#,,2#0.5g.2#,.2#,,,.,2#0.5g;0.5g,2#0.5g.52#Fig.5Effectsofthedosageofthedeslimingagent2#onthesolidcontentsandwatercontentsofrecoveredoil06121824302#/g1.00.90.80.70.60.5/%50403020/%62#Fig.6Effectsofthedosageofthedeslimingagent2#onrecoveryrateoftreatedsludge06121824302#/g9694929088/%0.30.40.50.60.70.82#/g96959493929190/%82#Fig.8Effectsofthedosageofthedehydratingagent2#onrecoveryrateoftreatedsludge,:72#Fig.7Effectsofthedosageofthedehydratingagent2#onthesolidcontentsandwatercontentsofrecoveredoil0.30.40.50.60.70.82#/g1.21.00.80.6403530252015/%/%337,2#1#6g、2#0.5g、1#0.6g2#6g,15.74%、0.74%、95.05%.2.230min、60℃、1000r/min,1#、2#,1.1,2#1,,.3a.:1#6g、2#0.5g、1#0.6g2#6g.b.2#:1#6g、2#0.5g、1#0.6g2#6g.2#1,0.81%0.74%,32.57%15.74%(),89.9%95.05%.致谢感谢渤海油田相关人员对本实验的大力支持,感谢对本论文完成给予过帮助的相关同仁!:[1],,.[J].,2001,12(2):25-27.HUANGSong-zhi,LIUZhen-kai,LAIXiao-xue.Thecurrentstatusofoilysludgeanditstreatmenttech-niqueinGudongOilfield[J].EnvironmentalProtectionofOil&GasFields,2001,12(2):25-27.(inChinese)[2],.[J].,2008,30(7):21–23.SHENMing-le,LIJin.Solventextractionforrecoveryofcrudeoilfromoilysludge[J].EnvironmentalPollution&Control,2008,30(7):21-23.(inChinese)[3].[J].,2006,29(2):39-45.SONGDan.Studyonthetreatmenttechnologyofoilysludge[J].EnvironmentalProtectioninPetrochemicalIndustry,2006,29(2):39-45.(inChinese)[4],,.[J].,1999,21(3):49-53.LIUGuang-quan,WANGRong-sha,XIAOYiao.Oilysludgetreatmenttechmologystudy[J].ChongqingEnvi-ronmentalScience,1999,21(3):49-53.(inChinese)[5],,,.[J].,2010,23(4):44-47.GUANYue-ming,ZHANGZhong-zhi,ZHANWei-mu,etal.Oilysludgedegradationbyland-farmingwithacommercialinocula[J].JournalofPetrochemicalUni-versities,2010,23(4):44-47.(inChinese)[6]WeissenfelsWD.RapidtestingsystemforassessingthesuitabilityofthebiologicalreclamationforPAHcontaminatedsoil[C].In:FifthEuropeanCongressonBioteehnology,1990:931-934.[7],,,.[J].,2010.20(1):20-22.ZHANYu-zhu,GAOHong-ge,ZHANGDa-song,etal.Studyonsolidificationtreatmenttechnologyforlow-oilsludge[J].EnvironmentalProtectionofOil&GasFields,2010,20(1):20-22.(inChinese)[8]SENGUPTAP,SAIKIAN.Oilfiledsludgeusedtomakebrick[J].AmericanCeramicSociety,2000,79(7):71-74.[9]SAIKIAN,SENGUPTAP.Cementitiouspropertiesofmetakaofin—normalPortlandceluentmixtureinthepresenceofpetroleumeffluenttreatmentplantsludge[J].CementandConcreteResearch,2002,32(11):1717-1724.[10],,,.[J].,2003,25(3):74-76.LIDan-mei,WANGYan-xia,YUQing-zhong,etal.ApplicationandresearchofprofilecontrolofoilySludge[J].Drilling&ProductionTechnology,2003,25(3):74-76.1Table1separateingefficiencyindifferentseparationagents1#2#/%0.810.74/%32.5715.74/%89.995.05(下转第20页)437RecoveryofsludgeoilinBohaioilfieldSHENXi-zhou1,2,WANGDao-nan2,YINXian-qing1,DUANJin-ting3,XIESheng-long2,ZHUJin-cheng2,ZHANGBao-sha21.CollegeofChemistryandEnvironmendalEngineering,YangtzeUniversity,Jingzhou434020,China;2.SchoolofChemicalEngineering&Pharmacy,WuhanInstituteofTechnology,Wuhan430074,China;3DagangOilFieldCompany,ChinaNationalPetroleumCorporation,Tianjin300280,ChinaAbstract:TheseparatingagentBohai2wasdevelopedusingtheoilysludgefromBohaiOilfieldbychemicalconditioning-mechanicalseparationmethod.AimedatthedisadvantageofseparatingagentBohai1,thecon-ditionswereoptimized.Theeffectsofdifferentconcentrationsofdifferentsingleagentsonthewatercontent,solidcontentoftheoillayerandtheoilrecoveryratewereresearched.Theresultsshowthattheoptimaleffi-ciencyofoilysludgetreatingachieveswhenthedehydratingagent1#is6g,thedeslimingagent1#is0.6g,thedeslimingagent2#is6gandthedehydratingagent2#is0.
本文标题:渤海油田含油污泥处理效果的改进
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