反硝化短程硝化厌氧氨氧化工艺处理晚期垃圾渗滤液的脱氮除碳性能王凡

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39820188ENVIRONMENTALSCIENCEVol.39No.8Aug.2018--123123123123123*1.2150092.2150093.215009-.-600mg·L-1COD<483mg·L-1NRR1.88kg·m3·d-1NRE90.3%COD>483mg·L-1C/N>0.8-NRR1.50kg·m3·d-1.-NH+4-N1100mg·L-1COD1150mg·L-1NRR1.37kg·m3·d-1NRRana15.6kg·m3·d-1NRE98.6%..X703.1A0250-3301201808-3782-07DOI10.13227/j.hjkx.2018012522018-01-282018-02-242016YFC0401103514782841992~E-mailwangfan@post.usts.edu.cn*E-mailyhuang@mail.usts.edu.cnTreatmentofOldLandfillLeachateviaaDenitrification-PartialNitritation-ANAMMOXProcessWANGFan123LUMing-yu123YINJi-qiang123LIXiang123HUANGYong123*1.SchoolofEnvironmentalScienceandEngineeringSuzhouUniversityofScienceandTechnologySuzhou215009China2.NationalandLocalJointEngineeringLaboratoryofMunicipalSewageResourceUtilizationTechnologySuzhouUniversityofScienceandTechnologySuzhou215009China3.InstituteofEnvironmentalBiotechnologySuzhouUniversityofScienceandTechnologySuzhou215009ChinaAbstractToresearchtheperformanceofremovingnitrogenandorganicsfromoldlandfillleachateviadenitrification-partialnitritation-ANAMMOXDN-PN-ANAMMOXprocessanintegratedreactorseededwithmatureANAMMOXsludgeandnitritationsludgeconnectedtoadenitrificationDNreactorwasstudied.Theresultshowedthatbeforethepre-denitrificationreactorwasconnectedthePN-ANAMMOXreactorachievedanitrogenremovalrateNRRof1.88kg·m3·d-1andanitrogenremovalefficiencyNREof90.3%whentheconcentrationofinfluentammonianitrogenandCODwere600mg·L-1and483mg·L-1respectively.TheNRRofthePN-ANAMMOXprocessdroppedto1.50kg·m3·d-1whentheconcentrationofinfluentCOD>483mg·L-1whichcorrespondstoC/N>0.8.TorelievetheinfluenceoforganicmatteronANAMMOXaDNreactorwasputinfrontofthePN-ANAMMOXreactor.TheDN-PN-ANAMMOXprocessachievedanNRRandNREof1.37kg·m3·d-1and98.6%respectivelyundertheconditionsofinfluentammonianitrogenandCODconcentrationsof1100mg·L-1and1150mg·L-1respectively.TheNRRofANAMMOXreached15.6kg·m3·d-1.Thewholesystemrealizedahighlyefficientanddeepremovalofnitrogenwithoutanyadditionalcarbonsource.Whentreatingoldlandfillleachatemostofthebiodegradableorganicscanberemovedbythesystem.KeywordsdenitrificationpartialnitritationanaerobicammoniaoxidationANAMMOXlandfillleachateorganicmatter1NH+4-NC/N312.anaerobicammoniaoxidationANAMMOX3~6ANAMMOXNH+4-NNO-2-NN28--partialnitritationPN、78.ANAMMOX11%NO-3-N910NH+4-N>1000mg·L-1NO-3-NNRE90%.denitrificationDNANAMMOXNO-3-NNRE.Miao11-PN-ANAMMOXSBRNRE90%ANAMMOXNRRana1.1kg·m3·d-1110mg·L-1CODNO-3-NNO-3-N60mg·L-1.Zhang12SNADNH+4-N1950mg·L-199%NRR0.15kg·m3·d-1Vo13SNAP1.4kg·m3·d-1NRR1.2kg·m3·d-190mg·L-1.ANAMMMOXSNAD、CANON、DEMONPN-ANAMMOX、DN-PN-ANAMMOX.、、1415.PN-ANAMMOX16.2kg·m3·d-117.PN-ANAMMOX.PN-ANAMMOX.11.1UASBPN-ANAMMOX1..DN-UASB1.8LPN-ANAMMOXPN、ANAMMOX10.25L1.4L1.92L.31~34℃.DNDNPN-ANAMMOXPNANAMMOXANAMMOXDNANAMMOXNO-3-N.1DN-PN-ANAMMOXFig.1FlowchartofDN-PN-ANAMMOXsystem1.2PN18NPR0.5kg·m3·d-1.ANAMMOXCSTR19CandidatusBrocadiasinicaKP721346-KP721365MLVSS/MLSS0.45.DN2.5mm.20.1.+NH4Cl.3873391Table1CharacteristicsofoldlandfillleachateNH+4-N/mg·L-1NO-2-N/mg·L-1NO-3-N/mg·L-1COD/mg·L-1BOD5/mg·L-1/mg·L-1/g·L-1pH1200~19000.1~0.50.1~0.51800~2200400~5006000~800016~187.7~8.11.320.NH+4-NNO-2-NN-1--NO-3-NMLVSS/MLSSCODDRB200BOD5BODTrak3020MpH、DO、WTWMulti9430.1.4PN-ANAMMOXDNPN-ANAMMOXANAMMOXNO-3-N.NH+4-N2.Ⅰ、ⅡNH+4-NNH+4-NNH+4-N..2NH+4-NTable2ComponentsandconcentrationsofinfluentammonianitrogenduringthetestNH+4-N/mg·L-1/dNH+4-N/%NH+4-N/%2080Ⅰ6001~534060703010006040Ⅱ1000~110054~928020100022.1PN-ANAMMOXPN-ANAMMOXNH+4-N600mg·L-1NRR1.1kg·m3·d-1NRE77%.29dNH+4-N20%.21.19~29dNH+4-N40%NH+4-N19~20d70mg·L-1.PN375L·h-1400L·h-1NH+4-N2UASB、COD、HRTFig.2ChangesininfluentandeffluentnitrogenCODinfHRTandpercentageoflandfillleachateintheinfluent15mg·L-148738--22PNNH+4-NAOBNH+4-N.19~29dNH+4-NNO-2-N13.78mg·L-116.35mg·L-1ANAMMOXHRT0.38d0.29dNLRPNNO-2-N/NH+4-N1.32.NRR19d1.23kg·m3·d-129d1.88kg·m3·d-1、22ANAMMOX.3NLR、NRRNREFig.3TrendsofNLRNRRandNRENH+4-N70%3NRR33dPN-ANAMMOX1.99kg·m3·d-1.30d~43dCOD483mg·L-1C/NTN0.8NH+4-NNO-2-NNRR39dNRR1.5kg·m3·d-1.PNANAMMOXANAMMOX.23ANAMMOXTOC/NH+4-N>0.4C/NTN>0.45ANAMMOX.30~40dNO-3-NNO-3-N19mg·L-110~30d4.ANAMMOX.4NO-3-NNO-3-NFig.4EffluentNO-3-Nintheoryandinreality2.2DN-PN-ANAMMOX40dDNPN-ANAMMOX1.DNANAMMOXNO-x-NDNDNNO-3-N.DN540~43dDN-PN-ANAMMOXNH+4-N、NO-2-NNO-3-NNRR1.5kg·m3·d-11.61kg·m3·d-1DNPN-ANAMMOX.44dNH+4-N100%NH+4-N.NO-3-NDNPNAOBPNNPRNH+4-N90mg·L-1.PN0.68m3·h-10.85m3·h-1NH+4-N30mg·L-1.47~53dNH+4-NNO-2-N15.2587339mg·L-15.4mg·L-1NO-3-N0NRE98.8%.54dNH+4-N1000mg·L-1HRT0.63dNH+4-N.ⅡNH+4-NPNANAMMOX.NO-3-NCODCOD.83dNH+4-N.NO-3-N0DNNO-x-NNRE.NH+4-N9.9mg·L-1TN<15mg·L-1NRE98.6%《》GB16889-2008.NRR1.37kg·m3·d-1ANAMMOXNRRana15.6kg·m3·d-1NRE.3NRRNRE.UASBPN-ANAMMOXANAMMOXNO-3-N、.5、COD、HRTFig.5ChangesininfluentandeffluentnitrogenCODinfHRTandpercentageoflandfillleachateintheinfluents31Table3ComparisonofsimilarresearchinrecentyearsTN/mg·L-1V/LHRT/dNRRANA/kg·m3·d-1NRRT/kg·m3·d-1NRET/%SNAD1950101.5—0.15a9912DN-PN-ANAMMOX1100330.77b1.10.52c9011ANAMMOXREACTOR650NH+4-N850NO-2-N100.1510—8924PN-ANAMMOX6007.51.10.590.558725PN-ANAMMOX100071.518.30.939326DN-PN-ANAMMOX110015.40.815.61.3798.61aSBR10%bANAMMOXHRTH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