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31320186EnvironmentalScienceandTechnologyVol．31No．3Jun．2018：2018-03－08：(SCJH-098);;(2017-019).：(1994-),,,,.：(1979-),,,,E-mail:1229646227@qq.com.A/O1，2，1，1，1，1（1.，331113;2.，232000）：A/O，A/O、TNTP，9。：COD，TN，NH4+-N，TP，SS16.0~428.0，2.0~40.6，0.3~35.8，0.4~5.0，107.0~157.0mg/L，0.4~58.5，0.4~20.0，0.1~30.7，0.1~1.0，3.0~18.0mg/L。COD，TN，NH4+-N，TP，SS64.6%，40.7%，79.3%，57.5%91.8%。A/O，，GB18918—2002《》，A/O。：A/O；；；；:X7:A:1674-4829（2018）03-0036-04ResearchonApplicationofHybridA/OProcessinPhosphorusandNitrogenRemovalinMunicipalWastewaterTreatmentPlantsKOUHai-tao1,ZHANGMing2,CAOWen－ping1,LIChao－ming1,CAOJun1,MATian－yi1(1.SchoolofWaterResourceandEnvironmentalEngineering,EastChinaUniversityofTechnology,Nanchang331113,China;2.SchoolofCollegeofEconomicsandManagement,AnhuiUniversityOfScienceAndTechnology,Huainan232000,China)Abstract:ToexplorethefeasibilityoftheapplicationofahybridA/Oprocessinmunicipalwastewatertreatmentplant,theremovalefficiencyoforganicmatter,totalnitrogen(TN)andtotalphosphorus(TP)inmunicipalwastewaterbyahybridA/Oprocesswasinvestigated.Morethan9monthsofproductiveexperimentswerecarriedout.TheresultsshowedthattheinfluentCOD,TN,NH4+-N,TP,SSconcentrationwere16.0~428.0,2.0~40.6,0.3~35.8,0.4~5.0,107.0~157.0mg/L.Theeffluentparameterwere0.4~58.5,0.4~20,0.1~30.7,0.1~1.0,3.0~18.0mg/L.TheaveragedremovalrateofCOD,TN,NH4+-N,TPandSSwere64.6%,40.7%,79.3%,57.5%and91.8%.ThehybridA/Oprocesshasagoodefficiencyoftheremovalofphosphorusandnitrogen,theeffluentwasclear,theeffluentwaterqualitiesweremorelowerthanpollutantdischargestandardofurbansewagetreatmentplants(GB18918—2002),whichindicatesthatthehybridA/Oprocessissuitableforapplicationinwastewatertreatmentplants.Keywords:HybridA/Oprocess;Activatedsludgeprocess;Biofilmprocess;Municipalwastewater;Phosphorusandnitrogenremoval0，。，、，：、、、、。、、，、[1-3]，。，[4-5]。313。A/O，A/O2，A（）O（），，NH4+-NTN，[6-7]。，；、[8]；、[9-10]。，，，，、，、[8,11]。A/O，。，A/O，AO，A/O，A/OCOD，TN，TP，SS，。11.1，（A）（O），1。A4h，O8h，2，。O，，（DO）3.0~3.5mg/L，200%，OMLSS2500~3200mg/L。A，OMLSS3500~4000mg/L，（）4h，100%。1.2500m3/d，。1。1.310（2h）；Origin9.0；[12]。22.1CODCOD2。2，ρ（COD）16.0~428.0mg/L，ρ（COD）0.4~58.5mg/L，64.6%；COD（12），COD，COD11ρ（COD）16.0428.0ρ（TN）2.040.6ρ（NH4+-N）0.335.8ρ（TP）0.45.0ρ（SS）107.0157.0pH（）7.08.6mg·L-1：，。200%100%50040030020010004080t/d1231201602002402802CODρ（COD）/(mg·L-1)A/O3720186。A/O，、、，。2.2TNTNNH4+-N34。3，ρ（TN）2.0~40.6mg/L,ρ（TN）0.4~20.0mg/L，TN53.9%~92.5%，TN70%，ρ（TN）13.5~18.5mg/L。A/OA、O（0.45~0.60cm），，TN。4，ρ（NH4+-N）0.3~35.8mg/L，ρ（NH4+-N）0.1~8.7mg/L，NH4+-N60.3%~98.5%，1NH4+-N81.1%~98.5%，480%，NH4+-NNH4+-N。A/O，（）。，。NH4+-N[13-14]。2.3TPTP5。5，ρ（TP）0.4~5.0mg/L，ρ（TP）0.1~1.0mg/L，TP，TP，90.4%，93.1%90.7%，TP。A/OA（）O（），，（0.45~0.60cm），，，TP。，TP，，。2.4SSA/OSS6。6，ρ（SS）107.0~157.0mg/L，ρ（SS）20mg/L，3TN4030201004080ρ（TN）/(mg·L-1)t/d1231201602002402804NH4+-N504030201004080ρ（NH4+-N）/(mg·L-1)123120160200240280t/d5TP6．04．53．01．504080ρ（TP）/(mg·L-1)123120160200240280t/d383136SS17515012510075502504080ρ（SS）/(mg·L-1)123120160200240280t/d90%。SS125mg/L，10mg/L。1，SS85.3%~90.3%，2，3，SS89.9%~94.8%，93.5%~97.4%，。3A/O，，、，、。A/O。（1）A/O，COD，TN，NH4+-N，TP16.0~428.0，2.0~40.6，0.3~35.8，0.4~5.0mg/L，0.4~58.5，0.4~20.0，0.1~30.7，0.1~1.0mg/L。COD，TN，NH4+-N，TP64.6%，40.7%，79.3%，57.5%。SS（10mg/L），。（2）A/O，TNTP40.7%57.5%，。（3），，，TP，，。[][1],,.[J].,2012,24(6):838-842.[2],,.[J].(),2015,33(6):36-40.[3],.[J].,2015(1):134-140.[4].[D].:,2012.[5],,.[J].(),2015,30(4):24-27.[6],,,.[J].,2015,41(11):82-85.[7],,,.[J].,2015,31(17):12-15.[8]CAOYong-feng,ZHANGChao-sheng,RONGHong-wei,etal.Theeffectofdissolvedoxygenconcentration(DO)onoxygendiffusionandbacterialcommunitystructureinmovingbedsequencingbatchreactor(MBSBR)[J].Waterresearch,2017,108:86-94.[9],,,.[J].,2017,11(11):5909-5916.[10].[J].,2017,42(4):96-99.[11],,,.[J].,2017,27(1):26-30.[12].[M].:,2002:352-553.[13]CAOWei-ping,ZHANGJian,WANGYin-mei,etal.Anultraviolet/biological(UV/B)reactorfortheremovalofnitrogenouscompoundsfromthesecondaryeffluentofwastewatertreatmentplants(WWTPs)[J].RSCadvance,2015,5:32239-32244.[14],,,.[J].(),2013,28(4):18-23.（）A/O39