给排水毕业设计外文翻译及原文.docx
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给排水毕业设计外文翻译及原文.docx
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给排水毕业设计外文翻译及原文
NutrientremovalinanA2O一MBRreactorwithsludgereduction
J.RajeshBanu,DoI DepartmentofCivilandEnvironmentalEngineeringSungllyunllwanUniversity,300,Chunchun-dong,Jangan-gu,Suwon-Si440-746,RepuhlicofKorea ARTICLEINFO Articlehistory: Received20July2008 Receivedinrevisedform11December2008 Accepted15December2008 Availableonline25February2009 Keywords: A2Oreactor MBR Nutrientremoval TMP ABSTRACT Inthepresentstudy,anadvancedsewagetreatmentprocesshasbeendevelopedbyincorporatingexcesssludgereductionandphosphorousrecoveryinanA2O-MBRprocess.TheA2O-MBRreactorwasoperatedatafluxof77LMHoveraperiodof270days.Thedesignedfluxwasincreasedstepwiseoveraperiodoftwoweeks.ThereactorwasoperatedattwodifferentMLSSrange.ThermochemicaldigestionofsludgewascarriedoutatafixedpH(11)andtemperature(75℃)for25%CODsolubilisation.Thereleasedpbospborouswasrecoveredbyprecipitationprocessandtheorganicswassentbacktoanoxictank.ThesludgedigestiondidnothaveanyimpactonCODandTPremovalefficiencyofthereactor.Duringthe270daysofreactoroperation,theMBRmaintainedrelativelyconstanttransmembranepressure.Theresultsbasedonthestudyindicatedthattheproposedprocessconfigurationhaspotentialtoreducetheexcesssludgeproductionaswellasitdidn'tdetonatedthetreatedwaterquality. @2008ElsevierLtd.Allrightsreserved. 1.Introduction Excesssludgereductionandnutrientsremovalarethetwoimportantproblemsassociatedwithwastewatertreatmentplant.MBRprocesshasbeenknownasaprocesswithrelativelyhighdecayrateandlesssludgeproductionduetomuchlongersludgeageinthereactor(Wenetal.,2004).SludgeproductioninMBRisreducedby28-68%,dependingonthesludgeageused(Xiaetal., 2008).However,minimizingthesludgeproductionbyincreasingsludgeageislimitedduetothepotentialadverseeffectofhighMLSSconcentrationsonmembrane(Yoonetal.,2004).Thisprob- lemcanbesolvedbyintroducingsludgedisintegrationtechniqueinMBR(Youngetal.,2007).Sludgedisintegrationtechniqueshavebeenreportedtoenhancethebiodegradabilityofexcesssludge(VlyssidesandKarlis,2004).Inoverall,thebasisforsludgereductionprocessesiseffectivecombinationofthemethodsforsludgedisintegrationandbiodegradationoftreatedsludge.Advancesinsludgedisintegrationtechniquesofferafewpromisingoptionsincludingultrasound(Guoetal.,2008),pulsepower(Choietal.,2006),ozone(Weemaesetal.,2000),thermal(Kimetal.,2003),alkaline(Lietal.,2008)acid(Kimetal.,2003)andthermochemical (VlyssidesandKarlis,2004).Amongthevariousdisintegrationtechniques,thermochemicalwasreportedtobesimpleandcosteffective(WeemaesandVerstraete,1998).Inthermal-chemicalhy- drolysis,alkalisodiumhydroxidewasfoundtobethemosteffectiveagentininducingcelllysis(Rockeretal.,1999). Conventionally,thenutrientremovalwascarriedoutinanA2Oprocess.Ithasadvantageofachieving,nutrientremovalalongwithorganiccompoundoxidationinasinglesludgeconfigurationusinglinkedreactorsinseries(Tchobanoglousetal.,2003).Thephosphoroesremovalhappensbysubjectingphosphorousaccumulatingorganisms(PAO)bacteriaunderaerobicandanaerobicconditions(AkinandUgurlu,2004).TheseoperatingproceduresenhancepredominancePAO,whichareabletouptakephosphorousinexcess.Duringthesludgepretreatmentprocessestheboundphosphorouswassolubilisedanditincreasesthephosphorousconcentrationintheeffluentstream(Nishimura,2001).So,itisnecessarytoremovethesolubilisedphosphorusbeforeitentersintomainstream.Besides,thereisagrowingdemandforthesustainablephosphorousresourcesintheindustrializedworld.Inmanydevelopedcountries,researchesarecurrentlyunderwaytorecoverthephosphoroesboundinthesludge'sofenhancedbiologicalphosphorusremovalsystem(EBPR).Thereleasedphosphorouscanberecoveredinusableproductsusingcalciumsaltsprecipitationmethod.Keepingthisfactinmind,inthepresentstudy,anewadvancedwastewatertreatmentprocessisdevelopedbyintegratingthreeprocesses,whichare: (a)thermochemicalpretreatmentinMBRforexcesssludgereduction(b)A2Oprocessforbiologicalnutrientremoval(c)Precoverythroughcalciumsaltprecipitation.Theexperimentaldataobtainedwerethenusedtoevaluatetheperformanceofthisintegratedsystem. 2.Methods 2.1.Wastewater Thesyntheticdomesticwastewaterwasusedastheexperimentalinfluent.Itwasbasicallycomposedofamixedcarbonsource,macronutrients(NandP),analkalinitycontrol(NaHCO3)andamicroelementsolution.Thecompositioncontained(L-')210mgglucose,200mgNH4C1,220mgNaHCO3,22一34mgKH2PO4,microelementsolution(0.19mgMnCl24H20,0.0018mgZnCl22H2O,0.022mgCuCl22H2O,5.6mgMgSO47H2O,0.88mgFeCl36H2O,1.3mgCaCl2·2H2O).Thesyntheticwastewaterwaspreparedthreetimesaweekwithconcentrationsof210±1.5mg/Lchemicaloxygendemand(COD),40±1mg/Ltotalnitrogen(TN)and5.5mg/Ltotalphosphorus(TP). 2.2.A2O-MBR TheworkingvolumeoftheA2O-MBRwas83.4L.Abafflewasplacedinsidethereactortodivideitintoanaerobic(8.4L)anoxic(25L)andaerobicbasin(50L).Thesyntheticwastewaterwasfeedintothereactorataflowrateof8.4L/h(Q)usingafeedpump.Aliquidlevelsensor,plantedinaerobicbasinofA2O-MBRcontrolledtheflowofinfluent.TheHRTofanaerobic,anoxicandaerobicbasinswere1,3and6h,respectively.Inordertofacilitatenutrientremoval,thereactorwasprovidedwithtwointernalrecycle(1R).IRl(Q=1)connectsanoxicandanaerobicandIR2(Q=3)wasbetweenaerobicandanoxic.Anaerobicandanoxicbasinswereprovidedwithlowspeedmixertokeepthemixedliquidsuspendedsolids(MLSS)insuspension.Intheaerobiczone,diffuserswereusedtogenerateairbubblesforoxidationoforganicsandammonia.Dissolvedoxygen(DO)concentrationintheaerobicbasinwasmaintainedat3.5mg/1andwasmonitoredcontinuouslythroughonlineDOmeter.Thesolidliquidseparationhappensin aerobicbasinwiththehelpoffiveflatsheetmembraneshavingaporesizeof0.23pm.Theareaofeachmembranewas0.1m2.Theywereconnectedtogetherbyacommontube.Aperistalticpump wasconnectedinthecommontubetogeneratesuctionpressure.Inthecommontubeprovisionwasmadetoaccommodatepressuregaugetomeasuretransmembranepressure(TMP)duringsuction.Thesuctionpumpwasoperatedinsequenceoftiming,whichconsistsof10minswitchon,and2minswitchoff. 2.3.Thermochemicaldigestionofsludge MixedliquorfromaerobicbasinofMBRwaswithdrawnattheratioof1.5%ofQ/dayandsubjectedtothermochemicaldigestion.ThermochemicaldigestionwascarriedoutatafixedpHof11(NaOH)andtemperatureof75℃for3h.Afterthermochemicaldigestionthesupernatantandsludgewereseparated.Thethermo-chemicallydigestedsludgewasamenabletofurtheranaerobicbio-degradation(VlyssidesandKarlis,2004),soitwassenttotheanaerobicbasinoftheMBR 2.4.Phosphorusrecovery Limewasusedasaprecipitanttorecoverthephosphorousinthesupernatant.Aftertherecoveryofprecipitantthecontentwassentbacktoanoxictankasacarbonsourceandalkalinitysupelementfordenitrification. 2.5.Chemicalanalysis COD,MLSS,TP,TNoftherawandtreatedwastewaterwereanalyzedfollowingmethodsdetailedin(APHA,2003).Theinfluentandeffluentammoniaconcentrationwasmeasuredusinganion-selectiveelectrode(TheretoOrion,Model: 95一12).Nitrateinthesamplewasanalyzedusingcadmiumreductionmethod(APHA,2003). 3.Resultsanddiscussion Fig.1presentsdataofMLSSandyieldobservedduringtheoperationalperiodofthereactor.OneoftheadvantagesofMBRreactorwasitcanbeoperatedinhighMLSSconcentration.ThereactorwasseededwithEBPRsludgefromtheKiheung,sewagetreatmentplant,Korea.ThereactorwasstartupwiththeMLSSconcentrationof5700mg/L.Itstartstoincreasesteadilywithincreaseinperiodofreactoroperationandreachedavalueof8100mg/Londay38.Fromthenonwards,MLSSconcentrationwasmaintainedintherangeof7500mg/LbywithdrawingexcesssludgeproducedandcalledrunI.Theobservedyields(Yobs)forexperimentswithoutsludgedigestion(runI)andwithsludgedigestionwerecalculatedandgiveninFig.1.TheYobsforrunIwasfoundtobe0.12gMLSS/gCOD.Itwascomparativelylowerthanavalueof0.4gMLSS/gCODreportedfortheconventionalactivatedsludgeprocesses(Tchoba-noglousetal.,2003).ThedifferenceinobservedyieldofthesetwosystemsisattributedtotheirworkingMLSSconcentration.AthighMLSSconcentrationtheyieldobservedwasfoundtobelow(Visva-nathanetal.,2000).AsaresultofthatMBRgeneratedlesssludge.ThepresentlyusedMLSSranges(7.5一10.5g/L)areselectedonthebasisoftherecommendationbyRosenbergeretal.(2002).Intheirstudy,theyreportedthatthegeneraltrendofMLSSincreaseonfoulinginmunicipalapplicationsseemstoresultinnoimpactatmediumMLSSconcentrations(7一12g/L). Thethermochemicalsludgedigestionwasstartedonday70bywithdrawingsludgeattheratioof1.5%Q/day.Thesludgedigestionperiodwasdividedintotwophasesnamely,runII(day70-139)andrunIII(day140-210).DuringrunII,theMLSSconcentrationinMBRwasmaintainedaround7500mg/LandforrunIIIitwasmaintainedaround10500mg/L.Bothofthesetworuns(IIandIII)demonstratetheroleofsludgedisintegrationincontrollingtheexcesssludgeproduction.TheYobsforrunIIandIIIwerefoundto
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