A2O型膜生物反应器污水处理工艺设计要点TextMark

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·d-1/℃/hSRT/hMLSS/mg·L-1/mg·L-1pH207.8~8.82.92.93.89.6388000~120003~46~8314020096No.3(SerialNo.140)Jun.2009CHINAMUNICIPALENGINEERING:2009-04-24(MBR)。A2/O。A2/OMBR,MBR,MBR。,20m3/dA2/OMBR(20081120~2009330),A2/OMBR。11.11。。(CODcr)、5d(BOD5)、(NH3-N)、(TN)、(TP)(SS)490、191、39、76、6.3、152mg/L。:(1∶1)MBR,;(3∶1)MBR,。1.2MBRUNA-620A。(PVDF);;0.1μm;17.5m2(25m2,17.5m2);准0.15mm×1.4m。1.3。(MLSS)6000~7000mg/L,20081120~20093301。1.4CODcr、BOD5、NH3-N、TN、TP、SS、、。[1]。22,20081120~200812311/d,20090101~200903300.33/d。1,1,1,2(1.,200125;2.,200336):,20m3/dA2/O(MBR),。,A。,30000m3/d,A2/O。,0.84/m3,。:;A2/O(MBR);;:X703:A:1004-4655(2009)03-0061-03A2/OACODcr/mg·L-120~4827.550BOD5/mg·L-16.6~10.09.510NH3-N/mg·L-10.7~3.51.85TN/mg·L-13.1~9.65.215TP/mg·L-10.2~0.50.40.5SS/mg·L-16~10810/NTU<0.1<0.1—/<5<530/·L-110361,A2/OMBR,。,A,,TNTP5.2mg/L0.4mg/L。3,,30000m3/d(12℃)A2/OMBR[2]。3.1,,A,,。3。3.24。3.3MLSS8000mg/L,5。BOD50.05~0.10kg/(kg·d)。3.4TN6。6,3∶1,TN12.5mg/L,。,。,TN,,。3.59min,1min,2。1)F軈=QS(1):F軈,m3/(m2·d);Q,m3/d;S,m2。2)Ff=F軈0.8(2):Ff,m3/(m2·d)。(1)(2),7。3.61):m(O)=0.55×ρB×Q+0.1×ρW×V+4.57×(ρN×Q-0.05ρN×Q)(3)-2.86×mot:m(O),kg/d;ρBBOD5,kg/m3;Q,m3/d;ρW,kg/m3;V,m3;ρNTN,kg/m3;mot,kg/d。(3),8。8/m3·d-1BOD5/kg·m-3TN/mg·L-1MLSS/mg·L-1/m3/kg·d-1300000.185010000a562512833:MLSS。/m3·d-1/m2·-1//m2/m3·m-2·d-130000252688672000.450.5672、56/kg·m-3·d-1/kg·kg-1·d-1CODcrBOD5CODcrBOD51.810.770.230.10++1.030.440.130.055:。TN/mg·L-1TN/%TN/mg·L-12∶1506716.53∶1507512.54∶1508010.04/m3/h125013750356254.51000116250.89.33/mg·L-1/mg·L-1/kg·d-1CODcr450<5012000BOD5180<105100NH3-N40<51050TN50<151050TP8<0.5225SS250<10720020093,,,:A2/O62·d-145.52452845.5245282110245280/455.024528022.20.20.922002496002250241200033216.911/t·a-1/·t-1/·a-1(NaClO)EFMCIP114.81500172224(C2H4O2)CIP57.383600206568(NaOH)pH41.6150062400(Na2S2O3)NaClO5.3535001871346/a12/·a-1577.1:0.68/kWh0.1:1.93/t46.0268.88a8.55.010.81800/(30d·)916.31310/m3·d-1BOD5/kg·m-3m/kg·d-1300000.183456//m3·h-1·-1/m3·d-1268873000015∶1m3·h-1m3·min-118816313.6920093,,,:A2/O15%,1kg0.277m3,:128330.277×0.15=308856m3/d,214.5m3/min。2):5~7m3/(h·)。9。N(4)。N=AQ(4):A,m3/h;Q,m3/h。20:1。,。MBR,、。3),512.8m3/min。3.7(5):m=ρB×Q×64%(5):m,kg/d;64%。10。10000mg/L,345.6m3。3.8tW=V×ρWmWT(6):tW,d;V,m3;ρW,kg/m3;mWT,kg/d。11625m3,:11625×103456=33.6d,34d。4,30000m3/d,A2/OMBR。1)11。70%,0.68/kWh,:33216.9×0.7×0.68×365=577/a。2)12。(EFM)1/7d,(CIP)0.5/a。3)13。:916.3365×30000=0.84/m3,。51)A2/OMBR。9.6h,38h,、,A。2),30000m3/dA2/OMBR0.84/m3。(1/m3)。:[1].[M].4.:,2002.[2].[M].2.:,2001.63(classA).BSfillerenhancednitrogenremovalefficiencysignificantly.Keywords:MembraneBioreactor(MBR);decentralizedreclamationunitforwastewatertreatment;BSfiller;hollowfibermembrane;A/O;A2/OOnImprovementPlanfromCombinedSystemtoSeparateSysteminShanghaiHanyangSewerageSystemZHANGHui1,WUYue2,XUCan-hua1,XUYue-jiang1(1.ShanghaiMunicipalSewageCo.Ltd.,Shanghai200070,China;2.ShanghaiMunicipalEngineeringDesignGeneralInstituteShanghai200092,China)Abstract:Themainimprovementmethod,fromcombinedseweragesystemtoseparateonehasbeenmentionedinthepaper.CombinedwithShanghaiHanyangSewerageSystemimprovementproject,theadvantages,possibilityandactualdifficultiesoftheimprovementprocesshavebeenemphasizedbytheauthor.Finally,theideationalplanofHanyangseparatesystemhasbeenintroduced.Keywords:seweragesystem;combinedsystem;seperatesystem;techniqueimprovementDesignPlanofBracingofFoundationPitinSuzhouRiverWaterSystemSewageInterceptionandTreatmentProjectYINGJun(ShanghaiUrbanConstructionDesignandResearchInstitute,Shanghai200125,China)Abstract:Thefourbracingplansofurbanfoundationpitprojectwerementionedincludingundergroundcontinuouswall,boredpilecombinedwithdeepmixingpile,steelcementsoilmixingwallandgravitybracingstructure.Aimingatthethreesewageinterceptionfacilities(DaWuchuan,ChangqiaoandMeilong)ofSuzhouRiverwatersystemsewageinterceptionandtreatmentproject,thedetaileddesignplanandconstructionwereputforwardbytheauthor.Keywords:sewageinterception;sewageinterceptionandtreatment;bracingoffoundationpitfacilities;designDesignPointsofA2/O-MBRWastewaterTreatmentProcessLINLin1,HUANGJin1,BAIHai-long1,ZHANGWei-xing21.ShanghaiUrbanConstructionDesignandResearchInstitute,Shanghai200125,China;2.AsahiKASEI,Shanghai200336,China)Abstract:Apilot-scaleMBRsystemusingthehollowfibermembranefromAsahiKASEIwithatreatmentscaleof20m3/dwasconstructedtostudythedeeptreatmentofmunicipalwastewater.Theresultsshowedthatthesystemransteadily.Theeffluentqualitymetorsurpassednational1stgrade(classA)standard.Basedonthepilottest,ageneralconceptualdesignofA2/O-MBRprocesssystemwithatreatmentscaleof30000m3/dwasperformed.Theunitwastewatertreatmentcostofthesystemwas0.84yuan/m3,whichwaslowerthantheothersimilarprocesses.Keywords:sewagetreatment;A2O-MBR;projectdesign;hollowfibermembraneTreatmentProcessandDesignPointsofSludgeDryingandBurningYUJue-jin(ShanghaiUrbanConstructionDesignandResearchInstitute,Shanghai200125,China)Abstract:Sludgehasbecomeoneofthemostimportantenvironmentalproblemsinfluencingthecitydevelopment.Torealizere

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