SBR中生物膜促进好氧颗粒化研究程媛媛

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SBR1212121212121.3410002.341000AGS。23d24d。AGS30d。。COD、TINTP90%、82%80%。TU992.3A1000-4602201801-0014-06GJJ150627XZG-16-08-08E-mail7770132146@163.comAerobicGranulationAcceleratedbyBiofilminaSequencingBatchReactorCHENGYuan-yuan12ZHAOJue12CHENGPeng12XUANXin-peng12ZHANGLi-nan12LONGBei121.JiangxiKeyLaboratoryofEnvironmentalGeotechnologyandEngineeringDisasterControlGanzhou341000China2.SchoolofArchitecturalandSurveying&MappingEngineeringJiangxiUniversityofScienceandTechnologyGanzhou341000ChinaAbstractThestrategythatattachedbiofilmwasscrappedintomixedliquorduringcultivationofaerobicgranularsludgeAGSbyselectionpressuremethodanditsinfluenceonthegranulationprocesswasexplored.Theproportionofgranulesincreasedalongwithattachedbiofilmscrappedintothemixedliquorduringthefirst23daysandgranulationrateincreasedquicklyaftertheelasticfillerwasremovedwhichleftalargeamountoffreebiofilmscrappedintothemixedliquorfromthe24thday.Theresultin-dicatedthatfreebiofilmplayedtheroleofprecursorandnucleiintheformationofAGSwheretheextra-cellularpolymericsubstancesnetworkfacilitatedtheconversionofloosebiofilmintocompactAGSbyhighselectionpressure.ThereforeAGSwascultivatedwithin30daysatlowtemperatureinwinterbythestrategy.Theexistenceofelasticfillergreatlyenhancedthestabilityofthesystemtoresistsludgebul-kingwhichreducedtheriskofstartupfailureevenifoperationalparameterwasimproperlycontrolledbyselectionpressuremethod.GoodperformanceofthereactorwasachievedwhereremovalratesofCOD·41·34120181CHINAWATER&WASTEWATERVol.34No.1Jan.2018TINandTPwereusuallymorethan90%82%and80%duringtheoperation.KeywordsaerobicgranularsludgebiofilmgranulationelasticfillerstabilityAGS、、1。2。SBRAGS1~23。45。6AGS1~35。。、AGS。78、910、1112、1314。、。、、。AGS1516AGS1。AGS17。。AGSSBRAGSAGSAGS。11.1SBR10.21L10cm130cmH/D1350%。1~23d1150cm、310m2/m324d。1.2~1.5cm/s。12℃、7℃、。SBRMLSS2500mg/L。6h、、441。W023d。W1W2。W1-W0W1-W2。1Tab.1Compositionofacycle/d/min/min/min/min1#1~333253022#4~633452023#7~833381724#9~1533431225#16~233348726#24~253350527#26~283352328#29~303353.51.529#31~423354121.218、、。COD、、TP600、306mg/LCOD2.4kg/m3·d。1.3COD、、、TP、SV、SVI、MLSS、·51·.watergasheat.comSBR341MLVSS19TIN、、、EPS17PS-PNLoweryEPS。22.13d423d。1。1~3d、13~15d。24d。1Fig.1Quantityofbiofilmandmasspercentageofstrippedbiofilm2。2=5mmFig.2Morphologicalchangesofsludgebar=5mm4d56。22dAGS30dAGS。5d36d。、AGS。2.22.2.1SV30/SV5SVI3。4dSVI11dSVI15d194.30mL/g。15dSVI3023.84mL/g。SVI25.81~37.34mL/g。SV30/SV58d59.09%~69.23%9~21d91.67%~57.14%2290%。20AGSSV30SV510%。36dAGS。3SV30/SV5SVIFig.3VariationofSV30/SV5andSVIduringcultivation2.2.2MLSSMLVSS/MLSSMLSSMLVSS/MLSS4。MLSS5d3.95~7.96g/LMLSSCOD。MLSS21d26d3.29g/L。AGS8dMLSS34·61·341.watergasheat.comd9.30g/L。MLSS7.08~7.34g/L。MLVSS/MLSS12d0.47~0.6013dMLVSS/MLSS0.81。8dMLVSS/MLSS210.24。13dMLVSS/MLSS0.31~0.5636d0.54~0.61。4MLSSMLVSS/MLSSFig.4VariationofMLSSandMLVSS/MLSSduringcultivation2.2.3EPSPN/PSEPSPN/PS5。EPS12d1243.83mg/gMLVSS。EPS2122EPS。EPS。5EPSPN/PSFig.5VariationofEPSandPN/PSduringcultivation22dEPS50.82~156.72mg/gMLVSS36d134.23~146.49mg/gMLVSS。PN/PS8d0.3~0.522dPN/PS0.40~1.5832dPN/PS0.71~0.84。EPSPN/PS、AGS。2.2.46a。29d22d2250%。24d30d90%。90%2330d。24d。30d1.2mm。6、Fig.6Variationsofgranulationrateaverageparticlesizeandsizedistributionduringcultivation6b93.82%~5.60%。0.3~0.6mm0.6~1、1~1.43、1.43~22~4mm。·71·.watergasheat.comSBR34124d1mm13%~22%。2.3COD4COD100mg/L90%。TP11d0.11~3.16mg/LTP1.0mg/L80%。116~183.50mg/LTIN5.30mg/L、82%3.2mg/LTIN0.70mg/L7。7TINFig.7ProfileofeffluentTINNH+4-NNO-3-NNO-2-NandremovalrateofTIN2.4AGS6AGS、AGS。1.2~1.5cm/s30~1min2.4kg/m3·d。24d。8~23dEPS86.78~95.56mg/gMLVSSPN/PS1.12~1.34EPS36dAGS134.23~142.72mg/gMLVSS。“”EPS6AGS8。AGS56AGSAGS。8Fig.8MechanismofrapidaerobicgranulationAGS。13~15d0.40kgCOD/kgMLSS·d0.62kgCOD/kgMLSS·d。。。“→→→AGS”AGS。3“→→→AGS”30d36dAGS。“”EPSAGS。1AdavSSLeeDJShowKYetal.AerobicgranularsludgerecentadvancesJ.BiotechnolAdv200826·81·341.watergasheat.com411-423.2.J.20163561914-1922.3ZhangQGHuJJLeeDJ.Aerobicgranularproces-sesCurrentresearchtrendsJ.BioresourTechnol201621074-80.4LimSJKimTH.ApplicabilityandtrendsofanaerobicgranularsludgetreatmentprocessesJ.Biomass&Bioenergy201360189-202.5PronkMKreukMKDBruinBDetal.Fullscaleper-formanceoftheaerobicgranularsludgeprocessforsew-agetreatmentJ.WaterRes201584207-217.6LiuYWangZWQinLetal.Selectionpressure-driv-enaerobicgranulationinasequencingbatchreactorJ.ApplMicrobiolBiotechnol20056726-32.7LiAJLiXYYuHQ.Aerobicsludgegranulationfa-cilitatedbyactivatedcarbonforpartialnitrificationtreat-mentofammonia-richwastewaterJ.ChemEngJ2013218253-259.8ZhouJHZhaoHHuMetal.Granularactivatedcar-bonasnucleatingagentforaerobicsludgegranulationeffectofGACsizeonvelocityfielddifferencesGACversusflocsandaggregationbehaviorJ.BioresourTechnol2015198358-363.9LiXMLiuQQYangQetal.EnhancedaerobicsludgegranulationinsequencingbatchreactorbyMg2+augmentationJ.BioresourTechnol200910064-67.10SajjadMKimKS.InfluenceofMg2+catalyzedgranu-larsludgeonfluxsustainabilityinasequencingbatchmembranebioreactorsystemJ.ChemEngJ2015281404-410.11.J.2017331513-19.12.J.201733178-13.13IvanovVWangXHStabnikovaO.StartercultureofP

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