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1121131.1500902.1001243.300051、SBR、。、18℃10℃SBR300μmMLSS6000mg/LSVI50~60mL/g。COD、PO3-4-P、NH+4-N85.8%、98.3%、99.2%。2hTN95.2%。X703A1000-4602201519-0038-058632012AA063406E-mailpyz@bjut.edu.cnCultivationofAerobicGranularSludgeunderLowTemperatureandItsApplicationtoTreatmentofMunicipalDomesticSewageGUOAn1PENGYong-zhen12WANGRan-deng1CHENGZhan-li131.StateKeyLaboratoryofUrbanWaterResourceandEnvironmentHarbinInstituteofTechnologyHarbin150090China2.KeyLaboratoryofBeijingforWaterQualityScienceandWaterEnvironmentRecoveryEngineeringEngineeringResearchCenterofBeijingBeijingUniversityofTechnologyBeijing100124China3.TianjinMunicipalEngineeringDesignandResearchInstituteTianjin300051ChinaAbstractTheaerobicgranularsludgewascultivatedinaSBRreactoroperatedinanaerobic/aero-bicalternatingmodeandwasappliedtotreatmunicipaldomesticsewageincoldregionunderlowtem-perature.Theaerobicgranularsludgewascultivatedsuccessfullyastheaverageparticlesizeofthegranu-larsludgewas300μmtheMLSSwas6000mg/LandthesludgeshowedgoodsettleabilityastheSVIkeptat50to60mL/gwhenthetemperaturereducedfrom18℃to10℃andkeptatlowvalueforalongtime.TheaerobicgranularsludgehadexcellentremovaleffectonCODPO3-4-PandNH+4-Nandtheaverageremovalrateswere85.8%98.3%and99.2%respectively.AdditionallyTNremovalrateof95.2%wasachievedbyadding2-houranoxicmixingtime.Keywordsaerobicgranularsludgelowtemperaturedomesticsewagepollutantsremoval·83·3119201510CHINAWATER&WASTEWATERVol.31No.19Oct.2015、、、。20~25℃1~318~10℃、SBRCOD、、。11.1SBR12cm42cm37cm4L。1/2。SBR46h5min90min210min1~29d30min30~47d20min48~80d15min81~136d10min。1。120~160L/h。201612840T/℃20406080100120140t/d1Fig.1Temperaturechangesduringoperationalstages1.2。COD、PO3-4-P、NH+4-N、TN122.8~383.5、1.7~5.5、42.7~62.8、47.3~68.2mg/L。COD1。MLSS4462mg/LMLVSS/MLSS0.58。1Tab.1Additionalcarbonsourceinvariousoperationalstages/d12~8081~8586~136/mg·L-104003002501.3NH+4-N、NO-3-N、NO-2-N、PO3-4-P、MLSS、MLVSS、SVCODTNTOC-VCPN/。22.12.1.123。a.1db.20dc.45dd.65de.85df.115d2Fig.2Morphologyofaerobicgranulesindifferentstages8101001000/滋m/%765432101d40d80d120d3Fig.3Particlesizedistributionindifferentstages50μm>200μm20d20~65d·93·.watergasheat.com3119100μm200μm80d、>200μm50%300μm。120d90μm600μm4。。。2.1.24。80000204060801001201401.00.80.60.40.20t/dMLVSS/MLSSMLSS、MLVSS/(mg·L-1)700060005000400030002000100020016012080400SVI/(mL·g-1)MLSSSVIMLVSSMLVSS/MLSS4Fig.4ChangeofMLSS/MLVSSandsettleability。1~29dMLSS4462mg/L7745mg/L。3020min5785mg/L。4815min。8110min400mg/L300mg/L86d250mg/L4923mg/L6000mg/L。MLVSSMLSS。1~20dMLVSS/MLSS0.580.800.89。SVI1~10d50~60mL/g。。2.22.2.1COD1COD352.30mg/LCOD70.20mg/L80.1%2~80d400mg/LCOD475.2~712.5mg/LCOD50~70mg/L70mg/L89.2%81~85d300mg/LCOD519.9~633.5mg/LCOD40~50mg/L91.7%86~136d250mg/LCOD413.3~633.5mg/LCOD50~60mg/L60mg/L85.8%。2.2.2PO3-4-PPO3-4-P5。1086020406080100120140100806040200t/d/%42PO4-P/(mg·L-1)3-5PO3-4-PFig.5PO3-4-PremovalindifferentoperationalstagesPO3-4-P50dPO3-4-P0~0.4mg/L0.07mg/L·04·3119.watergasheat.com98.3%。PO3-4-PA。2.2.3NH+4-NNH+4-NNH+4-N0~2.45mg/L0.50mg/L99.2%。NH+4-NNH+4-NA。DeKreuk520℃8℃20℃8℃610℃SBARCOD、NH+4-NPO3-4-P86.8、5.22.0mg/L84.5%、91.1%94.1%Bao710℃SBARCOD、NH+4-NPO3-4-P90.6%~95.4%、72.8%~82.1%95.8%~97.9%COD、NH+4-NPO3-4-P85.8%、99.2%98.3%。。2.310℃6。MLSS6110mg/L120L/h。COD、PO3-4-P、NH+4-N、TN612.80、5.49、62.75、63.47mg/L59.52、0、0、20.22mg/L。4035302520151050060120180240300360420250200150100500t/minNH4-NNO3-NTNNO2-NPO4-PCOD+--3-、/(mg·L-1)COD/(mg·L-1)6A/OA/O/AFig.6VariationofpollutantsduringA/OandA/O/Acycle30minCOD230.10mg/L66.62mg/L。CODCODPHA。COD68.79mg/LCODCOD59.52mg/L。VFAsPHAPO3-4-P32.48mg/LPHA30minPO3-4-P0.05mg/L。30minNH+4-NNH+4-N30~60minNH+4-NNH+4-NNH+4-NNH+4-N。NH+4-NNH+4-N。30min。NO-2-NNO-2-N16.19mg/LNO-3-N3.94mg/L。TN33.52mg/L20.22mg/LTN30min、。2.4、NH+4-NTN2h、、A/O/A。62hNO-2-NTNNO-3-NTN3.05mg/LTN95.2%。COD·14·.watergasheat.com3119。NO-2-N、NO-3-N、TNCODCODCOD。820~25℃///NH+4-NNO-3-NNH+4-NNO-2-NNO-2-NNO-3-N。CODCODCOD。3、SBR。10minMLSS6000mg/LSVI50~60mL/g300μm600μm。COD、PO3-4-P、NH+4-N85.8%、98.3%、99.2%NO-2-N。2hTNTN3.05mg/L95.2%。1TorregrossaMDiBellaGVivianiGetal.PerformancesofagranularsequencingbatchreactorGSBRJ.Wa-terSciTechnol2007558/9125-133.2LiuYQTayJHMoyBYP.Characteristicsofaerobicgranularsludgeinasequencingbatchreactorwithvaria-bleaerationJ.ApplMicrobiolBiotechnol2006715761-766.3LiuYLiuZWangFetal.Regulationofaerobicgranu-larsludgereformulationaftergranularsludgebrokenEffectofpolyaluminumchloridePACJ.BioresourTechnol2014158201-208.4./J.201531134-9.5DeKreukMKPronkMVanLoosdrechtMCM.Forma-tionofaerobicgranulesandconversionprocessesinanaerobicgranularsludgereactoratmoderateandlowtem-peraturesJ.WaterRes200539184476-4484.6.J.201244611-15.7BaoRYuSShiWetal.AerobicgranulesformationandnutrientsremovalcharacteristicsinsequencingbatchairliftreactorSBARatlowtemperatureJ.JHazardMater200916821334-1340.8.D.2014.1990-。E-mailguoan_mail@126.com2015-06-12·24·3119.watergasheat.com
本文标题:低温好氧颗粒污泥的培养及处理生活污水研究郭安
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