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AAO/12312121.3003922.3003923.5701001.5×104m3/dAAO+++A。AAOAAO、SSTPTN。。AAOTU992.3C1000-4602201722-0067-04ApplicationofAAO-oxidationDitch/FiberTurntableFilterinRenovationandExpansionProjectofWastewaterTreatmentPlantLIUZhen12BAOGuang-zhou3WANGSong12LIGuo-jin121.TianjinMunicipalEngineeringDesign&ResearchInstituteTianjin300392China2.TianjinEnterpriseKeyLaboratoryofInfrastructureDurabilityTianjin300392China3.ChinaConstructionSixthEngineeringDivisionCorp.Ltd.<SouthChina>Haikou570100ChinaAbstractThedesigncapacityoftherenovationandexpansionprojectofSanyaLizhigouWastewaterTreatmentPlantwas1.5×104m3/d.Consideringthewastewatercharacteristicsthecom-binedprocessofAAO-oxidationditchsecondarysedimentationtankcoagulationsedimentationtankandfiberturntablefilterwasadopted.TheprojecteffluentwasrequiredtomeetthefirstlevelBcriteriaspeci-fiedofGB18918-2002.TheAAO-oxidationditchwasusedtogetherwiththefirst-phaseoxidationditchthesecondarysedimentationtankandfiberturntablefilterhydraulicloadwerereducedviaseveralwayssuchasincreasingthediameterofthesecondarysedimentationtankbuildingcoagulativeprecipita-tiontankandturntablefilterandimprovingtheremovaleffectsofSSandTP.Besidestheabovemeth-odscarbonsourcedosingdevicewasbuiltinordertoimprovetheTNremovaleffect.Theoperationre-sultsshowedthattheprocesswasdesignedreasonablyandtheeffluentqualitymetthedesignstandard.KeywordsrenovationandexpansionofwastewatertreatmentplantAAO-oxidationditchcoagulationsedimentationfiberturntablefilter3.0×104m3/d1.5×104m3/d2011。3.97hm22.97hm21.0hm2。AAO+《》GB18918—2002A·76·3322201711CHINAWATER&WASTEWATERVol.33No.22Nov.2017。“”、“”、“”“”201612。“”“”。。11.13.0×104m3/d1.5×104m3/d、、、、、3.0×104m3/d1.5×104m3/d。1.5×104m3/d2.175×104m3/d1.45。1.2201412—20164GB18918—2002A、1。1、Tab.1Designinfluentandeffluentqualitymg·L-1CODBOD5SSNH3-NTPTN300150150353.540501010580.5152①、、、。②SSTP、SSTP。③BOD5TN。④、、。⑤、。⑥。31~43.11。粗格栅及进水泵房细格栅及旋流沉砂池AAO微曝氧化沟配水井及污泥泵房辐流式二沉池纤维转盘滤池接触池及回用水泵房巴氏计量槽进水排入三亚东河鼓风机房加氯间加药间污泥浓缩池污泥脱水机房至红沙污泥处理中心碳源投加间AAO氧化沟配水井及污泥泵房辐流式二沉池混凝沉淀池纤维转盘滤池接触消毒池中水送水泵房改造构(建)筑物一期构(建)筑物扩建构(建)筑物(1.5×104m3/d)扩建构(建)筑物(3.0×104m3/d)至中水管网(远期)1Fig.1Flowchartofrenovationandexpansionproject3.2、3.0×104m3/d。221.0m20mm75°2480m3/h162kPa37kW4114Nm3/min39.2kPa7.5kW21。3.3①AAO·86·3322.watergasheat.comAAO11.8×104m3/d1.247.0m×44.6m×7.0m6.0m2。4410mm4.0kW。41.8m2.0kW50r/min0.3m/s。42.5m3.1kW35r/min296120mm13~17m3/m·h0.3m/s。。422560m3/h5kPa3.2kW。AAO15.9d0.075kgBOD5/kgMLSS·d3.2g/L0.9kgDS/kgBOD510500m31.5h4.0h8.5h14h252kg/h6∶1100%~200%50%~100%。②12.175×104m3/d9.6m6m。321315m3/h65kPa11kW21140m3/h100kPa3.0kW。③22.175×104m3/d22m4.9m4.2m。1.19m3/m2·h3.52h0.82m3/m2·h5.11h。20m17.4%。④3.0×104m3/d1.5×104m3/d211110℃110℃1。290Nm3/min0.075MPa135kW。⑤BOD5/TN>3.5BOD5/TN=3.75、13.0×104m3/d10m3232150~200kg/h0.3MPa1.1kW。3.4、12.175×104m3/d33.2m×17.2m×6.0m2。①61s20.8m2.2kW14min43.0m0.37kW6.77m3/m2·h28.4m0.37kW141m21.0m60°。②3.0×104m3/d1.5×104m3/d2.0m1214.23m3/m2·h6.74m3/m2·h。12.0m1611.5m3/m2·h。·96·.watergasheat.comAAO/3322③43min。10m3232150~200kg/h0.3MPa1.1kW。3.5①112m4.7m。5tDS/d99.3%97%。21148m3/h200kPa7.5kW。②3.0×104m3/d1.5×104m3/d148m3/h22kW21110~30m3/h200kPa4.0kW2111.5m3/h0.6MPa1.5kW21。PAM12000L/h0.3%3×0.55+0.37kW。42016。20171—62。2Tab.2Actualeffluentqualitymg·L-1CODBOD5SSNH3-NTPTN2017118.262.24<40.970.3913.872017220.002.25<40.400.3913.822017316.902.02<40.600.4013.002017418.002.00<40.300.4012.802017511.401.55<40.060.3712.732017611.001.90<40.100.4011.3015.931.99<40.410.3912.9229733.8m3/d2A。56747.015671.09757.01318.91。1.79/m31.10/m3。61.5×104m3/d3.0×104m3/dAAO+++A。1.62M.2002.2GB50014—20062016S.2016.3.M.2005.4.AAOJ.2010262226-29.1988-。E-mail545829706@qq.com2017-06-13·07·3322.watergasheat.com
本文标题:AAO氧化沟纤维转盘滤池用于污水厂改扩建刘振
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