污水操作手册(可编辑优质文档)

1、污水操作手册（E）（可编辑优质文档）（可以直接使用，可编辑完整版资料，欢迎下载）DegussaSpecialtyChemicals(Shanghai)Co.,LtdIndustrialWastewaterTreatmentSystemOperationManualPACTEnvironmentalTechnologyCo.,Ltd.Contents6.1 ChapterOneGeneralPrincipleChapterTwoGeneralRequirementsOperationManagementSafeOperationRepairandMaintenanceChapterThreeTe

2、chnicalDesignandProcessFlowTechnicalDesignWasteQuantityWaterQualityStandardsofDischargedWaterQualityProcessFlowWasteDisposalProcessFlowDesignWasteDisposalProcessFlowSpecificationChapterFourDisposalStructure,EquipmentFunctionandDesignParametersChapterFiveFlowDistributionandBalancingduringWasteDisposa

3、lEquipmentsDailyOperationWasteDisposalCapacityAverageFlowofEveryMainWasteLiftingPumpChapterSixMainDisposalStructureandEquipmentDebugandOverallLinkedOperation(ByClearWater)PurposeConfirmationandPreparationBeforeTrialOperationElectromechanicalEquipmentUnitDebugMainTaskElectromechanicalEquipmentConnect

4、ionPipeFittingsCleaningandEquipmentPerformanceParameterConfirmationAirblowerandTransferPiping6.3.2.2AerationTankAirDiffuser6.3.2.3WasteLiftingPumpandTransferPipingSettingofEveryEquipmentsDischargeCapacityOverallLinkedOperation：ChapterSevenBiochemicalDisposalStructureDebuggingOperationTransferofAerob

5、icActivatedSludgeCultureandAcclimatizationofActivatedSludgeSpecialAttentionsandTestItemsduringTransfer,CultureandAcclimatizationofActivatedSludgeChapterEightSandFilterOperationFillingofSandFilterBackwashofSandFilterOperationofSandFilterChapterNineOperation,Round-InspectionandMaintenanceManagementofE

6、veryDisposalStructureandEquipmentSystemTargetDeterminingDailyRound-InspectionPeriodduringWasteDisposalDailyOperationofDisposalStructureandEquipmentOperationofEveryWaterTankWaterPumpAirblowerDosingEquipmentBiochemicalDisposalStructureSludgeDisposalChapterTenWater(Sludge)Sampling,TestingandAnalyzingWa

7、terSamplingandPreservingWaterSamplingWaterPreservingPollutionPropertyIndexofDailyWasteWaterQualityAnalyzingGeneralWaterQualityTestItemandMethodMainWasteQualityAnalysisMethodWaterQualityTestManagementWaterQualityTestSafeOperationandMaintenanceChapterElevenElectricOperationAppendixAppendix1WasteDispos

8、alSystemPIDChartChapterOneGeneralPrinciple1.1 Inordertostrengthenmanagementonwastedisposalequipment,techniqueandwaterquality,guaranteenormaloperationofwastedisposalstructureandelectromechanicalequipmentandensuredischargedwaterafterdisposaluptoregulatedwaterqualitystandardsforenvironmentprotection,he

9、retodrawupthismanual;Inadditiontomeetingthisregulation,operation,maintenanceandothersafeoperationofwastedisposalequipmentshouldalsocomplywithregulationsincurrentnationalcriteriaandstandards.ChapterTwoGeneralRequirements1.1.1 OperationManagementPersonnelinchargeofoperationmanagementshouldbefamiliarwi

10、thdisposaltechnique,structureandequipmentfunction,operationrequirementsforeveryequipmentandrelevanttechnologyspecificationsofthiswastedisposalsystem;Periodicallyround-inspecttheoperationofstructure,electromechanicalequipment,instrumentanddevice;Makeoperationrecordsandwaterqualityanalysisrecordswitha

11、ccuratedataontime;Keepstructuresliketankandcontainerandequipmentwatersurfacefreeofanyfloaterandtankwallanddischargeweirnotchcleanandintact;Keepeverymechanicalequipmentandpipefittingsclean,nooil,waterandairleakage;Keepfloorofdisposalsystemclean,nostackedmessandnowetCheckelectromechanicalequipmentperi

12、odicallyaccordingtodifferentrequirements,addorreplacelubricantorsolidlubricantandmakeperiodicmaintenanceandoverhaultoensureequipmentundergoodoperation.1.1.2 SafeOperationOperatorandrepaireronthepostmustaccepttechnologytrainingandstartworkingaftertestedforqualification;Cutoffelectricitybeforerepairin

13、gelectromechanicalequipmentandstartoperationafterhangamaintenancetagontheswitch;Onrainyorsnowydays,operatorshouldconcernmoreaboutsafeoperationtopreventslidingwhenround-inspectingoroperatingdisposalstructure;Operatoroneverypostshouldhavesafetylaborprotectionwearingforsafeprotection;Nowipingtorunningp

14、artofequipmentwhencleaningelectromechanicalequipmentandsurroundings;Personnotasoperatorisforbiddentostartandstopelectromechanicalequipmentofthisdisposalsystem.1.1.3 RepairandMaintenanceOperationmanagementpersonnelandmaintenancepersonnelshouldbefamiliarwithelectromechanicalequipmentsmaintenanceregula

15、tions;Makeperiodicinspection,maintenanceandanti-corrosiontreatmenttovariousvalve,grate,ladder,piping,bracketandcoverboardofdisposalstructureandequipmentandrepairdamagedlightingintime;Frequentlycheckandfastenconnectingpartsinvariousequipmentandreplaceconsumablepartincouplerperiodically;Makeopen&close

16、testforvariouspipingvalvesperiodicallyandaddlubricanttoleadscrew;Checklimitswitchofelectricgatevalveandmanual&electricinterlockdevice,cleanelectriccontrolcabinetandtestvarioustechnologicalspecificationsperiodically;Afteracertainperiodofoperation,checkairproofatwaterpumpfilingoroilsealingwithnecessar

17、ytreatment;Besidesdailymaintenance,airblower,waterpumpandothermechanicalequipmentshouldhavedisassemblyoverhaulasthefollowingoperationtime:airblowerwithaccumulatedoperationtime10000h;centrifugalpumpwithaccumulatedoperationtimeof4000h;divingpumpwithaccumulatedoperationtimeof5000h;andthosewaterpumpsand

18、airblowersnotusedfrequentlyshouldhaveadisassemblyoverhaulonceeverythreeyears;Cleanconnectionpipingandopenchannelbetweendisposalstructureandequipmentonceeveryyear;Makeroutinemaintenanceandrepairaccordingtorequirementsineveryelectromechanicalequipmenttsoperationspecifications.ChapterThreeWasteDisposal

19、TechnicalDesignandProcessFlow3.1 TechnicalDesign：ThiswastedisposalsystemisusedforindustrialwastedisposalinDegussaSpecialtyChemicals(Shanghai)Co.,Ltd.Thetechnicaldesignforwastedisposalincludesthefollowingsevenparts:Industrialwastecollection,flowadjustmentandhomogenization;Wastecoagulationreactionandd

20、epositionWastePHadjustmentWastebiochemicaltreatmentDisposedwaterfiltering；WatermeasureddischargeSludgedisposal.3.1.1 Wastequantity:3.1.2 Industrialwastedisposalcapacityisdesignedas20m3/d；designedflowis2m3/HWastequalityindex：Basedonrelevantdatasuppliedbyowner,industrialwastesqualityisdesignedasPH:4.0

21、-7.0CODcr:5000-20000mg/L;BOD5:500-4000mg/L;SS:3500-16000mg/L;StandardsofdischargedwaterqualityAsrequiredbyowner,wasteshouldreachthefollowingstandardsafterdisposal：CODcr=5002000mg/LSSRemovalratio95%;Cr1.5mg/L;Zn5.0mg/L;Cu1.0mg/LPb1.0mg/LAs0.5mg/LWasteuptostandardswillbedischargedintomunicipalpipenetw

22、ork.2.2 Processflowandspecifications2.2.1 SpecificationsonprocessflowPleaserefertotheattachedprocessflowchartforwastedisposalprocessflowandthebriefdescriptionisasfollows:IndustrialwastewillbeliftedintoadjustmenttankS-2801forqualityandquantityadjustmentthroughinletpipeline.Withonejetblenderinthetank,

23、partofoutletwaterfromliftingpumpP-2801inadjustmenttankflowsbacktoadjustmenttankforblendingtopreventsuspendedsubstanceinthewastetodepositinthetank.TheliftingpumpinadjustmenttankisstartedorstoppedbyliquidleveltransmitterLICA2801Sinthetank.Whenliquidinthetankreacheshighlevel,liftingpumpinitwillstartaut

24、omaticallyandlifttheliquidinadjustmenttankintocoagulationtankR-2810A.Andwhenliquidinthetankreacheslowlevel,liftingpumpwillstopautomatically.Whetherliquidathigh-highlevelorlow-lowlevel,systemwillsendoutalarmautomatically.CoagulantFeCl3willbeaddedintocoagulationtankR-2810AandblendedbyblenderA-2810Asoa

25、stomixwasteandcoagulantquickly.Meanwhile,aPHmeterPH2810AisinstalledincoagulationtanktotestPHvalueinthetank.LiquidfromcoagulationtankflowsintoreactiontankR-2810B,intowhichlimemilkwillbeadded.ThroughblenderA-2810B,limemilkandwastewillbemixedquicklyandanotherPHmeterisinstalledinreactiontankPH2810Btocon

26、troltheinputamountoflimemilk.Byadjustinginputamountoflimemilk,heavymetalandpartoforganicsubstanceinwastewillreactwithcoagulanttoformflocwithinanappropriatePHrange.LiquidfromreactiontankflowsintoflocculationtankR-2810C,inwhichmacromoleculeflocculantPAMwillbeadded.ThroughblenderA-2801C,PAMwillmixwithw

27、astequickly.FlocanddepositinwastewillbecomelargerflocthrougheffectofnettingandbridginggeneratedafterflocculantPAMdissolves.LiquidfromflocculationtankflowsintoverticalflowtypedepositiontankV-2315forliquidandsolidseparation.Theupperclearliquidflowstothefollowingprocessforfurtherdisposalthroughoverflow

28、weirwhilesludgedepositstothesludgefillerandisliftedintosludgetankV-2820forfurtherdisposalthroughsludgepumpP-2815indepositiontank.LiquidfromdepositiontankflowsintoPHadjustmenttankV-2840,inwhichH2SO4willbeadded.ThroughblenderA-2840,H2SO4willmixwithwastequickly.APHmeterPH2840isinstalledinthetanktocontr

29、oltheinputamountofH2SO4toensurePHvalueinthetankwithintherangeof6.58.5.AliftingpumpP-2840isinstalledinPHadjustmenttankandthepumpisstartedandstoppedbyliquidlevelswitchLSA2840Vinthetank.WhenliquidinPHadjustmenttankreacheshighlevel,liftingpumpinitwillstartautomaticallyandliftthewasteinadjustmenttankinto

30、SBRtankS-2850orS-2855.Andwhenliquidinthetankreacheslowlevel,liftingpumpinthetankwillstopautomatically.Whetherliquidathigh-highlevelorlow-lowlevel,systemwillsendoutalarmautomatically.LiquidfromPHadjustmenttankflowsintoSBRtank(abbreviationofSequencingBatchReactorActivatedSludgeProcess).Thedifferencebe

31、tweenSBRandgeneralactivatedsludgeprocessliesinthewasteflowingintoabiologicalreactiontankfordifferentoperationaccordingtotimesequenceratherthanflowingintoeverydisposalunitinsequence.Itsbasicoperationprocessiscomposedof5procedures:inlet,reaction,deposition,outletandstand-by.Onecyclestartsfromwasteinle

32、tandfinishestillstand-by.Duringthiscycle,alltheprocessesaremadeinareactiontankfilledwithaeration,whichgoesroundandroundceaselesslysoastorealizewastedisposal.TherearetwoSBRtanksforalternateoperationandtherearethreeairblowerswithtwoinuseandoneforbackup.TwoairblowersseparatelysupplyairtotwoSBRtanks.The

33、operationprocessesforeverycycleisshownasfollows:Waterinlet/aeration5.56HDeposition1.5HWateroutlet0.5HStand-by00.5HTheresidualsludgeinSBRreactiontanksS-2850/S-2855willbetransferredintosludgetankV-2820fordisposal.LiquidfromSBRtankflowsintobuffertankV-2860.IfwaterfromSBRmeetsdischargestandards,itwillbe

34、dischargedintomunicipalpipenetworkthroughdischargepumpP-2865.Ifitdoesnotmeetdischargestandards,itwillbeliftedbyliftingpumpP-2860inbuffertankintosandfilterF-2860forfurtherdisposal.LiftingpumpinbuffertankisstartedandstoppedbyliquidleveltransmitterLICA2860Vinbuffertank.Whenliquidinbuffertankreacheshigh

35、level,liftingpumpinitwillstartautomaticallyandliftthewasteintankintosandfilter.Andwhenliquidinthetankreacheslowlevel,liftingpumpinthetankwillstopautomatically.Whetherliquidathigh-highlevelorlow-lowlevel,systemwillsendoutalarmautomatically.WaterfromsandfilterwillbetestedbynephelometerTURB2860F.Ifturb

36、iditynotreachesdischargestandards,waterwillflowintoadjustmenttankS-2801forfurtherdisposalwhileifturbidityreachesstandards,waterwillflowintodischargetankV-2865.Ifwaterindischargetankreachesdischargerequirements,itwillbedischargedintomunicipalpipenetworkthroughdischargepump.Ifnot,operatorcancallfortan

37、kcartoshipoutside.Afteroperatingaperiodoftime,sandfilterwillhavelargerresistanceinitsfilteringlayersopressuredifferencebetweeninletandoutletwaterinfilterwillbecomelargerandlarger.Ifpressuredifferencereachesat0.05Mpa,pressuredifferenceswitchPDS2860FwillsendsignaltoPLCandsystemwillsendoutalarmtooperat

38、orforbackwash.Waterfrombackwashwillbedischargedintoditch.Afterbackwashcompletedbyhand,theprocessoffilteringwillcontinue.AftersludgeinsludgetankV-2820isblendedandcondensedbyblenderA-2820,theupperclearliquidisdischargedintoditchandcondensedsludgewillbetransferredtoframetypefilterpressF-2830fordehydrat

39、ionthroughscrewpumpP-2830.Afterdehydration,filtercakewillbeshippedoutsidewhilefilteredliquiddischargedintoditch.SludgescrewpumpP-2830iscontrolledbyliquidlevelswitchLSA2820V,stoppedatlowliquidlevel,startedbyhandathighliquidlevelandalarmsentoutathigh-highliquidlevel.Wastedischargedintoditchwillbecolle

40、ctedintowellS-2820andliftedintoadjustmenttankforfurtherdisposalthroughliftingpumpP-2802incollectionwell.TheliftingpumpincollectionwelliscontrolledbyliquidlevelswitchLS2802S,stoppedatlowliquidlevelandstartedathighliquidlevel.ChapterFourDisposalStructure,EquipmentFunctionandDesignParametersWastedispos

41、alprojectwillinvolveincoordinationofmanydisposalstructures,suchasadjustmenttank,SBRtank,buffertankanddischargetank,etc,electromechanicalequipment,suchasliftingpump,airblower,blender,sandfilter,frametypefilterpress,etcandtransferpipelineandadjustmentequipmentbetweenstructureandequipmenttorealizevario

42、usfunctionsandreachtheexpectedrequirements.Thefollowingsarevariousdisposalstructure,electromechanicalequipmentfunctionandrelevantparametersofthisproject:4.1 Mainstructureandequipment:4.1.1 Adjustmenttank(S-2801concretetankonthegroundFunction：Usedforwastestorageandquality&quantitybalancing,installedw

43、ithjetblenderinside.Quantity:1unitDimension：3000X3000X4250mmEffectivevolume:30m3Effectivestationaryperiod:1.5dayBlendingstyle:JetblendingRelevantequipmentinthetankincludeAdjustmenttankliftingpump(P-2801)Quantity:1setModel:CO500/30KDeliverylift:20mPower：3.0kWManufacturer：LOWARA4.1.1.2Floatballlevelme

44、ter(LSA2801S)Model:MAC-3Quantity:1unitManufacturer：DalianMAC4.1.1.3 Applicabletemperature：0C-50CLiquidleveltransmitter(LICA2801S)Model：LU11Quantity：1unitManufacturer：FLOWLINEApplicabletemperature：-40C-70C4.1.2Coagulationtank(R-2810A,carbonsteelFRPanti-corrosionFunction：Offerspaceforcoagulationreacti

45、onbetweencoagulantandwaste.Quantity：1unitDimension：650X1450X1500mmEffectivevolume：1.0m3Effectivestationaryperiod:0.5hCoagulationtankblender(A-2810A,Carbonsteellinedwithrubber)Function：MakecoagulantandwastemixquicklyModel：JB350X1500Quantity：1unitMotorpower：0.37KWRotationspeed136r/minLeafdiameter：350m

46、m4.1.2.2PHmeter(PH2810A)Model：InPro3200/120/pt1000+2050eQuantity：1unitMeasurerange014ManufacturerMETTLERTOLEDOReactiontank(R-2810B,CarbonsteelFRPanti-corrosionFunction：OfferspaceforchemicalreactionbetweenlimemilkandsubstanceinwasteandgeneratedeposithereQuantity：1unitDimension：1300X1450X1500mmEffecti

47、vevolume：2.0m3Effectivestationaryperiod:1.0hReactiontankblender(A-2810B,Carbonsteellinedwithrubber)Function：Makelimemilkandwastemixquickly.Model：JB450X1500Quantity：1unitMotorpower：0.37KWRotationspeed115r/minLeafdiameter450mmModel:PHmeter(PH2810B)InPro3200/120/pt1000+2050eQuantity:1unitMeasurerange01

48、4Manufacturer：METTLERTOLEDO4.1.3 Flocculationtank(R-2810C,CarbonsteelFRPanti-corrosionFunction：Offerspaceforflocculationreactionbetweenflocculantandwaste.Quantity:1unitDimension：650X1450X1500mmEffectivevolume：1.0m3Effectivestationarytime：0.5hFlocculationtankblender(A-2810C,Carbonsteellinedwithrubber

49、)Function：MakeflocculantandwastemixquicklyModel：JB350X1500Quantity：1unitMotorpower：0.55KWRotationspeed136r/minLeafdiameter350mm4.1.5Depositiontank(V-2815,Carbonsteelepoxyanti-corrosionFunction：ForliquidandsolidseparationinwasteQuantity：1unitDimension：42200X4100mmEffectivevolume：7.0m34.1.5.1 Effectiv

50、estationarytime：3.5hRelevantequipmentinthetankincludeCentralpipeindepositiontankFunction：ReduceflocmovingQuantity：1setMaterial：Carbonsteelepoxyanti-corrosionDimension：4200mmManufacturerPACT4.1.5.2Sludgepump(P-2815)Function：Usedtotransfersludgeatthebottomoftanktosludgetank.Quantity：1setModel：6661A3-3

51、EB-CFlow：5m3/hDeliverylift：15mManufacturerARO4.1.6 PHadjustmenttanlc(V-2840,CarbonsteelFRPanti-corrosionFunction:EnsurewasteflowingintoSBRbiologicalreactiontankwithneutralPHvalueQuantity：1unitDimension：41800X3800mmEffectivevolume：9.0m3Effectivestationarytime：4.5hRelevantequipmentinthetankincludeLift

52、ingpumpinPHadjustmenttank(P-2840)Function：LiftwasteinPHadjustmenttankintoSBRtankQuantity：1setModel：CO350/05Deliverylift：8mPower0.55kWManufacturer：LOWARA4.1.6.2Floatballlevelmeter(LSA2801V)Model：MAC-3Quantity：4unitsManufacturerDalianMACApplicationtemperature：0C-50CPHadjustmenttankblender(A-2840,Carbo

53、nsteellinedwithrubber)Function：MakeH2SO4andwastemixquicklyandensureneuralPHvalueofwasteforbiochemicaltreatment.Model：JB700X3800Quantity：1unitMotorpower：3.0KWRotationspeed100r/minLeafdiameter700mmFunction：PHmeter(PH2840)UsedtocontrolinputamountofH2SO4intoPHadjustmenttank.InPro3200/120/pt1000+2050e1un

54、it014METTLERTOLEDOModel：Quantity：MeasurerangeManufacturerSBRtank(S-2850/2855ConcretetankonthegroundFunction:Amainstructureforwastebiologicaltreatmentbymakinguseofactivatedsludgemethod.Asabiologicalreactor,SBRtankisusedtodegradeorganicsubstanceinthewastecontinuouslywithinareactioncycle.Quantity:2unit

55、sforalternateoperationEquipmentdimension：2500X2500X4500mm,concretestructure;Effectivevolume:3Veffective=50m；AerationtankaveragestationaryperiodT=25hr,(calculatedasflowof2m3/hr)Aeratortype:PerforatedpipeaerationQuantity:2setsRelevantequipmentinthetankinclude4.1.7.1 SBRtanksludgepump(P-2850)Function：U

56、sedtotransferresidualsludgeinSBRtankintosludgetankQuantity:1setModel：CO350/05Flow：5m3/hDeliverylife：8mPower0.55kWManufacturerLOWARAAirblower(B2850A/B/C)Function：SupplyairintoSBRtankforbiologicaltreatmentQuantity;3units(2inuse1backupModel;SSR-80Windrate：2.50m3/minOutletwindpressure0.50kgf/cm24.0kWMot

57、orpower:Manufacturer:ShandongZhanghuang4.1.7.2 Floatballlevelmeter(LS2850S/LS2855S)Model:MAC-32unitsManufacturer：DalianMACApplicabletemperature：0C-50CQuantity:Function：DecantorUsedtodischargeupperclearliquidafterdisposalinSBRtank.2setsUPVCPACTQuantity：Material：ManufacturerApplicabletemperature0C-50CBuffertank(V-2860Concretetankontheground)Function：Usedtostorewasteafterbiochemicaltreatmentandadjustwaterquantitybeforefiltering.Ifwastemeetsdischargestandard,itwillbedischargedbydischargepumpandifn