污水操作手册(E)(常用版)

污水操作手册(E)（常用版）(可以直接使用，可编辑完整版资料，欢迎下载）

污水操作手册(E)（常用版）(可以直接使用，可编辑完整版资料，欢迎下载）DegussaSpecialtyChemicals(Shanghai)Co.,LtdIndustrialWastewaterTreatmentSystemOperationManualPACTEnvironmentalTechnologyCo.,Ltd.

ContentsChapterOne GeneralPrincipleChapterTwoGeneralRequirementsOperationManagementSafeOperationRepairandMaintenanceChapterThreeTechnicalDesignandProcessFlowTechnicalDesignWasteQuantityWaterQualityStandardsofDischargedWaterQualityProcessFlowWasteDisposalProcessFlowDesignWasteDisposalProcessFlowSpecificationChapterFourDisposalStructure,EquipmentFunctionandDesignParametersChapterFiveFlowDistributionandBalancingduringWasteDisposalEquipment’sDailyOperationWasteDisposalCapacityAverageFlowofEveryMainWasteLiftingPumpChapterSix MainDisposalStructureandEquipmentDebugandOverallLinkedOperation（ByClearWater）PurposeConfirmationandPreparationBeforeTrialOperationElectromechanicalEquipmentUnitDebugMainTaskElectromechanicalEquipmentConnectionPipeFittingsCleaningandEquipmentPerformanceParameterConfirmationAirblowerandTransferPipingAerationTankAirDiffuserWasteLiftingPumpandTransferPipingSettingofEveryEquipment’sDischargeCapacityOverallLinkedOperation：ChapterSeven BiochemicalDisposalStructureDebuggingOperationTransferofAerobicActivatedSludgeCultureandAcclimatizationofActivatedSludgeSpecialAttentionsandTestItemsduringTransfer,CultureandAcclimatizationofActivatedSludgeChapterEightSandFilterOperation8.1 FillingofSandFilter8.2 BackwashofSandFilter8.3 OperationofSandFilterChapterNineOperation,Round-InspectionandMaintenanceManagementofEveryDisposalStructureandEquipmentSystemTargetDeterminingDailyRound-InspectionPeriodduringWasteDisposalDailyOperationofDisposalStructureandEquipmentOperationofEveryWaterTankWaterPumpAirblowerDosingEquipmentBiochemicalDisposalStructureSludgeDisposalChapterTen Water(Sludge)Sampling,TestingandAnalyzingWaterSamplingandPreservingWaterSamplingWaterPreservingPollutionPropertyIndexofDailyWasteWaterQualityAnalyzingGeneralWaterQualityTestItemandMethodMainWasteQualityAnalysisMethodWaterQualityTestManagementWaterQualityTestSafeOperationandMaintenanceChapterEleven ElectricOperationAppendixAppendix1 WasteDisposalSystemPIDChart

ChapterOneGeneralPrincipleInordertostrengthenmanagementonwastedisposalequipment,techniqueandwaterquality,guaranteenormaloperationofwastedisposalstructureandelectromechanicalequipmentandensuredischargedwaterafterdisposaluptoregulatedwaterqualitystandardsforenvironmentprotection,heretodrawupthismanual;Inadditiontomeetingthisregulation,operation,maintenanceandothersafeoperationofwastedisposalequipmentshouldalsocomplywithregulationsincurrentnationalcriteriaandstandards.

ChapterTwoGeneralRequirementsOperationManagementPersonnelinchargeofoperationmanagementshouldbefamiliarwithdisposaltechnique,structureandequipmentfunction,operationrequirementsforeveryequipmentandrelevanttechnologyspecificationsofthiswastedisposalsystem;Periodicallyround-inspecttheoperationofstructure,electromechanicalequipment,instrumentanddevice;Makeoperationrecordsandwaterqualityanalysisrecordswithaccuratedataontime;Keepstructuresliketankandcontainerandequipmentwatersurfacefreeofanyfloaterandtankwallanddischargeweirnotchcleanandintact;Keepeverymechanicalequipmentandpipefittingsclean,nooil,waterandairleakage;Keepfloorofdisposalsystemclean,nostackedmessandnowet；Checkelectromechanicalequipmentperiodicallyaccordingtodifferentrequirements,addorreplacelubricantorsolidlubricantandmakeperiodicmaintenanceandoverhaultoensureequipmentundergoodoperation.SafeOperationOperatorandrepaireronthepostmustaccepttechnologytrainingandstartworkingaftertestedforqualification;Cutoffelectricitybeforerepairingelectromechanicalequipmentandstartoperationafterhangamaintenancetagontheswitch;Onrainyorsnowydays,operatorshouldconcernmoreaboutsafeoperationtopreventslidingwhenround-inspectingoroperatingdisposalstructure;Operatoroneverypostshouldhavesafetylaborprotectionwearingforsafeprotection;Nowipingtorunningpartofequipmentwhencleaningelectromechanicalequipmentandsurroundings;Personnotasoperatorisforbiddentostartandstopelectromechanicalequipmentofthisdisposalsystem.RepairandMaintenance：Operationmanagementpersonnelandmaintenancepersonnelshouldbefamiliarwithelectromechanicalequipment’smaintenanceregulations;Makeperiodicinspection,maintenanceandanti-corrosiontreatmenttovariousvalve,grate,ladder,piping,bracketandcoverboardofdisposalstructureandequipmentandrepairdamagedlightingintime;Frequentlycheckandfastenconnectingpartsinvariousequipmentandreplaceconsumablepartincouplerperiodically;Makeopen&closetestforvariouspipingvalvesperiodicallyandaddlubricanttoleadscrew;Checklimitswitchofelectricgatevalveandmanual&electricinterlockdevice,cleanelectriccontrolcabinetandtestvarioustechnologicalspecificationsperiodically;Afteracertainperiodofoperation,checkairproofatwaterpumpfilingoroilsealingwithnecessarytreatment;；Besidesdailymaintenance,airblower,waterpumpandothermechanicalequipmentshouldhavedisassemblyoverhaulasthefollowingoperationtime:airblowerwithaccumulatedoperationtime10000h;centrifugalpumpwithaccumulatedoperationtimeof4000h;divingpumpwithaccumulatedoperationtimeof5000h;andthosewaterpumpsandairblowersnotusedfrequentlyshouldhaveadisassemblyoverhaulonceeverythreeyears;Cleanconnectionpipingandopenchannelbetweendisposalstructureandequipmentonceeveryyear;Makeroutinemaintenanceandrepairaccordingtorequirementsineveryelectromechanicalequipment’soperationspecifications.

ChapterThreeWasteDisposalTechnicalDesignandProcessFlowTechnicalDesign：ThiswastedisposalsystemisusedforindustrialwastedisposalinDegussaSpecialtyChemicals(Shanghai)Co.,Ltd.Thetechnicaldesignforwastedisposalincludesthefollowingsevenparts:Industrialwastecollection,flowadjustmentandhomogenization;Wastecoagulationreactionanddeposition；WastePHadjustment；Wastebiochemicaltreatment；Disposedwaterfiltering；Watermeasureddischarge；Sludgedisposal.Wastequantity:Industrialwastedisposalcapacityisdesignedas：20m3/d；designedflowis2m3/HWastequalityindex： Basedonrelevantdatasuppliedbyowner,industrialwaste’squalityisdesignedas：PH: 4.0-7.0CODcr: 5000-20000mg/L；BOD5: 500-4000mg/L；SS: 3500-16000mg/L；3.1.3Standardsofdischargedwaterquality： Asrequiredbyowner,wasteshouldreachthefollowingstandardsafterdisposal：CODcr =500~2000mg/L；SS Removalratio95%；Cr ≤1.5mg/L；Zn ≤5.0mg/L；Cu ≤1.0mg/LPb ≤1.0mg/LAs ≤0.5mg/LWasteuptostandardswillbedischargedintomunicipalpipenetwork. ProcessflowandspecificationsSpecificationsonprocessflow：Pleaserefertotheattachedprocessflowchartforwastedisposalprocessflowandthebriefdescriptionisasfollows:IndustrialwastewillbeliftedintoadjustmenttankS-2801forqualityandquantityadjustmentthroughinletpipeline.Withonejetblenderinthetank,partofoutletwaterfromliftingpumpP-2801inadjustmenttankflowsbacktoadjustmenttankforblendingtopreventsuspendedsubstanceinthewastetodepositinthetank.TheliftingpumpinadjustmenttankisstartedorstoppedbyliquidleveltransmitterLICA2801Sinthetank.Whenliquidinthetankreacheshighlevel,liftingpumpinitwillstartautomaticallyandlifttheliquidinadjustmenttankintocoagulationtankR-2810A.Andwhenliquidinthetankreacheslowlevel,liftingpumpwillstopautomatically.Whetherliquidathigh-highlevelorlow-lowlevel,systemwillsendoutalarmautomatically.CoagulantFeCl3willbeaddedintocoagulationtankR-2810AandblendedbyblenderA-2810Asoastomixwasteandcoagulantquickly.Meanwhile,aPHmeterPH2810AisinstalledincoagulationtanktotestPHvalueinthetank.LiquidfromcoagulationtankflowsintoreactiontankR-2810B,intowhichlimemilkwillbeadded.ThroughblenderA-2810B,limemilkandwastewillbemixedquicklyandanotherPHmeterisinstalledinreactiontankPH2810Btocontroltheinputamountoflimemilk.Byadjustinginputamountoflimemilk,heavymetalandpartoforganicsubstanceinwastewillreactwithcoagulanttoformflocwithinanappropriatePHrange.LiquidfromreactiontankflowsintoflocculationtankR-2810C,inwhichmacromoleculeflocculantPAMwillbeadded.ThroughblenderA-2801C,PAMwillmixwithwastequickly.FlocanddepositinwastewillbecomelargerflocthrougheffectofnettingandbridginggeneratedafterflocculantPAMdissolves.LiquidfromflocculationtankflowsintoverticalflowtypedepositiontankV-2315forliquidandsolidseparation.TheupperclearliquidflowstothefollowingprocessforfurtherdisposalthroughoverflowweirwhilesludgedepositstothesludgefillerandisliftedintosludgetankV-2820forfurtherdisposalthroughsludgepumpP-2815indepositiontank. LiquidfromdepositiontankflowsintoPHadjustmenttankV-2840,inwhichH2SO4willbeadded.ThroughblenderA-2840,H2SO4willmixwithwastequickly.APHmeterPH2840isinstalledinthetanktocontroltheinputamountofH2SO4toensurePHvalueinthetankwithintherangeof6.5~8.5.AliftingpumpP-2840isinstalledinPHadjustmenttankandthepumpisstartedandstoppedbyliquidlevelswitchLSA2840Vinthetank.WhenliquidinPHadjustmenttankreacheshighlevel,liftingpumpinitwillstartautomaticallyandliftthewasteinadjustmenttankintoSBRtankS-2850orS-2855.Andwhenliquidinthetankreacheslowlevel,liftingpumpinthetankwillstopautomatically.Whetherliquidathigh-highlevelorlow-lowlevel,systemwillsendoutalarmautomatically.LiquidfromPHadjustmenttankflowsintoSBRtank(abbreviationofSequencingBatchReactorActivatedSludgeProcess).ThedifferencebetweenSBRandgeneralactivatedsludgeprocessliesinthewasteflowingintoabiologicalreactiontankfordifferentoperationaccordingtotimesequenceratherthanflowingintoeverydisposalunitinsequence.Itsbasicoperationprocessiscomposedof5procedures:inlet,reaction,deposition,outletandstand-by.Onecyclestartsfromwasteinletandfinishestillstand-by.Duringthiscycle,alltheprocessesaremadeinareactiontankfilledwithaeration,whichgoesroundandroundceaselesslysoastorealizewastedisposal.TherearetwoSBRtanksforalternateoperationandtherearethreeairblowerswithtwoinuseandoneforbackup.TwoairblowersseparatelysupplyairtotwoSBRtanks.Theoperationprocessesforeverycycleisshownasfollows:Waterinlet/aeration 5.5~6HDeposition 1.5HWateroutlet 0.5HStand-by 0~0.5HTheresidualsludgeinSBRreactiontanksS-2850/S-2855willbetransferredintosludgetankV-2820fordisposal.LiquidfromSBRtankflowsintobuffertankV-2860.IfwaterfromSBRmeetsdischargestandards,itwillbedischargedintomunicipalpipenetworkthroughdischargepumpP-2865.Ifitdoesnotmeetdischargestandards,itwillbeliftedbyliftingpumpP-2860inbuffertankintosandfilterF-2860forfurtherdisposal.LiftingpumpinbuffertankisstartedandstoppedbyliquidleveltransmitterLICA2860Vinbuffertank.Whenliquidinbuffertankreacheshighlevel,liftingpumpinitwillstartautomaticallyandliftthewasteintankintosandfilter.Andwhenliquidinthetankreacheslowlevel,liftingpumpinthetankwillstopautomatically.Whetherliquidathigh-highlevelorlow-lowlevel,systemwillsendoutalarmautomatically.WaterfromsandfilterwillbetestedbynephelometerTURB2860F.Ifturbiditynotreachesdischargestandards,waterwillflowintoadjustmenttankS-2801forfurtherdisposalwhileifturbidityreachesstandards,waterwillflowintodischargetankV-2865.Ifwaterindischargetankreachesdischargerequirements,itwillbedischargedintomunicipalpipenetworkthroughdischargepump.Ifnot,operatorcancallfortankcartoshipoutside.Afteroperatingaperiodoftime,sandfilterwillhavelargerresistanceinitsfilteringlayersopressuredifferencebetweeninletandoutletwaterinfilterwillbecomelargerandlarger.Ifpressuredifferencereachesat0.05Mpa,pressuredifferenceswitchPDS2860FwillsendsignaltoPLCandsystemwillsendoutalarmtooperatorforbackwash.Waterfrombackwashwillbedischargedintoditch.Afterbackwashcompletedbyhand,theprocessoffilteringwillcontinue. AftersludgeinsludgetankV-2820isblendedandcondensedbyblenderA-2820,theupperclearliquidisdischargedintoditchandcondensedsludgewillbetransferredtoframetypefilterpressF-2830fordehydrationthroughscrewpumpP-2830.Afterdehydration,filtercakewillbeshippedoutsidewhilefilteredliquiddischargedintoditch.SludgescrewpumpP-2830iscontrolledbyliquidlevelswitchLSA2820V,stoppedatlowliquidlevel,startedbyhandathighliquidlevelandalarmsentoutathigh-highliquidlevel. WastedischargedintoditchwillbecollectedintowellS-2820andliftedintoadjustmenttankforfurtherdisposalthroughliftingpumpP-2802incollectionwell.TheliftingpumpincollectionwelliscontrolledbyliquidlevelswitchLS2802S,stoppedatlowliquidlevelandstartedathighliquidlevel.

ChapterFourDisposalStructure,EquipmentFunctionandDesignParameters Wastedisposalprojectwillinvolveincoordinationofmanydisposalstructures,suchasadjustmenttank,SBRtank,buffertankanddischargetank,etc,electromechanicalequipment,suchasliftingpump,airblower,blender,sandfilter,frametypefilterpress,etcandtransferpipelineandadjustmentequipmentbetweenstructureandequipmenttorealizevariousfunctionsandreachtheexpectedrequirements.Thefollowingsarevariousdisposalstructure,electromechanicalequipmentfunctionandrelevantparametersofthisproject:4.1Mainstructureandequipment：4.1.1Adjustmenttank（S-2801concretetankontheground）Function： Usedforwastestorageandquality&quantitybalancing,installedwithjetblenderinside.Quantity：1unitDimension： 3000X3000X4250mmEffectivevolume：30m3Effectivestationaryperiod：1.5dayBlendingstyle： JetblendingRelevantequipmentinthetankinclude：4.1.1.1Adjustmenttankliftingpump（P-2801）Quantity： 1setModel： CO500/30KFlow： 7m3/hDeliverylift： 20mPower： 3.0kWManufacturer： LOWARA4.1.1.2Floatballlevelmeter(LSA2801S)Model： MAC-3Quantity： 1unitManufacturer： DalianMACApplicabletemperature：0℃-50℃4.1.1.3Liquidleveltransmitter(LICA2801S)Model： LU11Quantity： 1unitManufacturer： FLOWLINEApplicabletemperature：-40℃-70℃4.1.2Coagulationtank（R-2810A，carbonsteelFRPanti-corrosion）Function： Offerspaceforcoagulationreactionbetweencoagulantandwaste.Quantity：1unitDimension： 650X1450X1500mmEffectivevolume： 1.0m3Effectivestationaryperiod：0.5h4.1.2.1Coagulationtankblender（A-2810A，Carbonsteellinedwithrubber）Function： MakecoagulantandwastemixquicklyModel： JB350X1500Quantity：1unitMotorpower： 0.37KWRotationspeed： 136r/minLeafdiameter： 350mm4.1.2.2PHmeter(PH2810A)Model： InPro3200/120/pt1000+2050eQuantity： 1unitMeasurerange： 0~14Manufacturer： METTLER

TOLEDO4.1.3Reactiontank（R-2810B，CarbonsteelFRPanti-corrosion）Function： OfferspaceforchemicalreactionbetweenlimemilkandsubstanceinwasteandgeneratedeposithereQuantity：1unitDimension： 1300X1450X1500mmEffectivevolume： 2.0m3Effectivestationaryperiod： 1.0h4.1.3.1Reactiontankblender（A-2810B，Carbonsteellinedwithrubber）Function： Makelimemilkandwastemixquickly.Model： JB450X1500Quantity：1unitMotorpower： 0.37KWRotationspeed： 115r/minLeafdiameter： 450mm4.1.3.2PHmeter(PH2810B)Model： InPro3200/120/pt1000+2050eQuantity： 1unitMeasurerange： 0~14Manufacturer： METTLER

TOLEDO4.1.4Flocculationtank（R-2810C，CarbonsteelFRPanti-corrosion）Function： Offerspaceforflocculationreactionbetweenflocculantandwaste.Quantity：1unitDimension： 650X1450X1500mmEffectivevolume： 1.0m3Effectivestationarytime：0.5h4.1.4.1Flocculationtankblender（A-2810C，Carbonsteellinedwithrubber）Function： MakeflocculantandwastemixquicklyModel： JB350X1500Quantity：1unitMotorpower： 0.55KWRotationspeed： 136r/minLeafdiameter： 350mm4.1.5Depositiontank（V-2815，Carbonsteelepoxyanti-corrosion）Function： ForliquidandsolidseparationinwasteQuantity：1unitDimension： φ2200X4100mmEffectivevolume： 7.0m3Effectivestationarytime：3.5hRelevantequipmentinthetankinclude：4.1.5.1CentralpipeindepositiontankFunction： ReduceflocmovingQuantity： 1setMaterial： Carbonsteelepoxyanti-corrosionDimension： φ200mmManufacturer： PACT4.1.5.2Sludgepump(P-2815)Function： Usedtotransfersludgeatthebottomoftanktosludgetank.Quantity： 1setModel： 6661A3-3EB-CFlow： 5m3/hDeliverylift： 15mManufacturer： ARO4.1.6PHadjustmenttank（V-2840，CarbonsteelFRPanti-corrosion）Function: EnsurewasteflowingintoSBRbiologicalreactiontankwithneutralPHvalueQuantity：1unitDimension： φ1800X3800mmEffectivevolume： 9.0m3Effectivestationarytime：4.5hRelevantequipmentinthetankinclude：4.1.6.1LiftingpumpinPHadjustmenttank（P-2840）Function： LiftwasteinPHadjustmenttankintoSBRtankQuantity： 1setModel： CO350/05Flow： 6m3/hDeliverylift： 8mPower： 0.55kWManufacturer： LOWARA4.1.6.2Floatballlevelmeter(LSA2801V)Model： MAC-3Quantity： 4unitsManufacturer： DalianMACApplicationtemperature：0℃-50℃4.1.6.3 PHadjustmenttankblender（A-2840，Carbonsteellinedwithrubber）Function： MakeH2SO4andwastemixquicklyandensureneuralPHvalueofwasteforbiochemicaltreatment.Model： JB700X3800Quantity：1unitMotorpower： 3.0KWRotationspeed： 100r/minLeafdiameter： 700mm4.1.6.4PHmeter(PH2840)Function： UsedtocontrolinputamountofH2SO4intoPHadjustmenttank.Model： InPro3200/120/pt1000+2050eQuantity： 1unitMeasurerange： 0~14Manufacturer： METTLER

TOLEDO4.1.7 SBRtank（S-2850/2855Concretetankontheground）Function:Amainstructureforwastebiologicaltreatmentbymakinguseofactivatedsludgemethod.Asabiologicalreactor,SBRtankisusedtodegradeorganicsubstanceinthewastecontinuouslywithinareactioncycle.Quantity： 2unitsforalternateoperationEquipmentdimension： 2500X2500X4500mm，concretestructure;Effectivevolume： Veffective=50m3； Aerationtankaveragestationaryperiod： T=25hr，（calculatedasflowof2m3/hr）Aeratortype: PerforatedpipeaerationQuantity： 2setsRelevantequipmentinthetankinclude：4.1.7.1SBRtanksludgepump（P-2850）Function： UsedtotransferresidualsludgeinSBRtankintosludgetankQuantity: 1setModel： CO350/05Flow： 5m3/hDeliverylife： 8mPower： 0.55kWManufacturer： LOWARA4.1.7.2Airblower(B2850A/B/C)Function： SupplyairintoSBRtankforbiologicaltreatmentQuantity； 3units（2inuse1backup）Model； SSR-80Windrate：2.50m3/minOutletwindpressure： 0.50kgf/cm2Motorpower： 4.0kWManufacturer： ShandongZhanghuang4.1.7.3Floatballlevelmeter(LS2850S/LS2855S)Model： MAC-3Quantity： 2unitsManufacturer： DalianMACApplicabletemperature： 0℃-50℃4.1.7.4DecantorFunction： UsedtodischargeupperclearliquidafterdisposalinSBRtank.Quantity： 2setsMaterial： UPVCManufacturer： PACTApplicabletemperature： 0℃-50℃4.1.8Buffertank(V-2860Concretetankontheground)Function：Usedtostorewasteafterbiochemicaltreatmentandadjustwaterquantitybeforefiltering.Ifwastemeetsdischargestandard,itwillbedischargedbydischargepumpandifnot,itwillbefiltered.Quantity： 1unitDimension： 2600X1000X4500mmEffectivevolume： 10m3Effectivestationarytime：5hRelevantequipmentinthetank：4.1.8.1Buffertankliftingpump(P-2860)Function： LiftliquidfromSBRtankintosandfilterforfiltering.Quantity： 1setModel： CO500/22Flow： 2m3/hDeliverylift： 20mPower： 2.2kWManufacturer： LOWARA4.1.8.2Liquidleveltransmitter(LICA2860V)Model： LU11Quantity： 1unitManufacturer： FLOWLINEApplicabletemperature： -40℃-70℃4.1.9Sandfilter(F-2860)Function： Filtersuspendedsubstancegeneratedbybiochemicaldisposal.Dimension： φ600X2600mmDesignedemptytowerflowrate： 7m/hFilteringlayerheight： 1000mm；Filteringmaterialspecification： 1.0-2.0mmquartzsandRelevantequipmentinthetankinclude：4.1.9.1Pressuredifferenceswitch(PDS2860F)Quantity： 1setMeasurerange： 0.02~0.1MPaManufacturer： ShanghaiFarEastMeter4.1.9.2Nephelometer(TURB2860F)Quantity： 1setTransmitter： T53A4A2N，220VAC，4~20MA，2RelaySensor： 8320T1A0C3NN,0~100NTUManufacturer： USGLI4.1.10Dischargetank(V-2865Concretetankontheground)Function：Storedisposedwaste.Ifitmeetsdischargestandard,itwillbedischargedintomunicipalpipenetworkandifnot,itwillbedischargedintowastetanktrucktobeshippedoutside.Quantity： 1unitDimension： 2600X2000X4500mmTotalvolume： V总=23m3；Effectivevolume： 20m3 Averagestationaryperiod：T=10hr，（Calculatedaccordingtoaveragedischargecapacity2m3/hr）Relevantequipmentinthetankinclude：4.1.10.1Dischargepump（P-2865）Quantity： 1setModel： CO500/22Flow： 15m3/hDeliverylift： 15mPower： 2.2kWManufacturer： LOWARA4.1.10.2Liquidleveltransmitter(LICA2865V)Model： LU11Quantity： 1unitManufacturer： FLOWLINEApplicabletemperature： -40℃-70℃4.1.10.3Electromagneticflowmeter(FIQ)Manufacturer： SIEMENSModel：7MQ5751-7DA11-1CB0/7ME5038-2AA12-1AA0/7MQ5941-7DA4Quantity： 1setSludgetank(V-2820CarbonsteelFRPanti-corrosion）Function：Usedforsludgestorageandcondensation.Quantity： 1unitDimension： φ2200X3300mmEffectivevolume： 10m3Relevantequipmentinthetankinclude：4.1.11.1Sludgetransferpump（P-2830）Quantity： 1setModel： G50-1Flow： 6m3/hDeliverylift： 6BARPower： 4.0kWManufacturer： TianjinPumpandMachinery4.1.11.2Floatballlevelmeter(LSA2820V)Model： MAC-3Quantity： 3unitsManufacturer： DalianMACApplicabletemperature：0℃-50℃4.1.11.3Sludgetankblender（A-2820，Carbonsteellinedwithrubber）Function:Byblending,makesludgecondensed.Model： NG2.2Quantity： 1unitMotorpower： 0.55KWRotationspeed： 0.19r/min4.1.11.4Electroconnectingpressuregauge(PS2830P)Model： YXC-100Quantity： 1unitMeasurerange： 0~1.0MPaManufacture： ShanghaiAutomationInstrumentationFrametypefilterpress(F-2830)Function：Usedinsludgedehydration.Model： XAZ40/800-UKQuantity： 1unitFilteringarea： 40M2Filteringroomvolume： 626LManufacturer： HangzhouBetter 4.1.13 Dosingdevice4.1.13.1 FeCl3slot(V-2870)Quantity：1setDimension： 1M3Material： PE4.1.13.1.1 FeCl3measuringpump(P-2870)Quantity： 1setModel： GM0050Flow： 50L/hDeliverylift： 10barPower： 0.25kWManufacturer： ShanghaiHansheng4.1.13.1.2 Floatballlevelmeter(LSA2870V)Model： MAC-3Quantity： 1unitManufacturer： DalianMAC4.1.13.2Limeslot(V-2871)Quantity：1setDimension： φ1000X1400mmMaterial： CarbonsteelManufacturer： PACT4.1.13.2.1Blender（A-2871，Carbonsteelepoxy）Model： JB1000X1400Quantity：1unitMotorpower： 0.37KWRotationspeed： 136r/minLeafdiameter： 200mm4.1.13.2.2 Limepump(P-2871)Quantity： 1setModel： 66605J-344Flow： 1.5M3/hDeliverylift： 2barManufacturer：ARO4.1.13.2.3 Floatballlevelmeter(LSA2871V)Model： MAC-3Quantity： 1unitManufacturer： DalianMAC4.1.13.3 PAMslot(V-2872)Quantity：1setDimension：φ1070X1370mmMaterial：PE4.1.13.3.1PAMblender（A-2872，Carbonsteelepoxy）Model： KJB1000Quantity：1unitMotorpower： 0.37KWRotationspeed： 136r/minLeafdiameter： 200mm4.1.13.3.2 PAMmeasuringpump(P-2872)Quantity： 1setModel： GM0170Flow： 170L/hDeliverylift： 7barPower： 0.25kWManufacturer：ShanghaiHansheng4.1.13.3.3Floatballlevelmeter(LSA2872V)Model： MAC-3Quantity： 1unitManufacturer： DalianMAC4.1.13.4 Antifoamagentslot(V-2873)Quantity：1setDimension：1M3Material：PE4.1.13.4.1 Antifoamagentmeasuringpump(P-2873)Quantity： 1setModel： GM0025Flow： 25L/hDeliverylift： 10barPower： 0.25kWManufacturer：ShanghaiHansheng4.1.13.4.2 Floatballlevelmeter(LSA2873V)Model： MAC-3Quantity： 1unitManufacturer： DalianMAC4.1.13.5Nutritionalagentslot(V-2874)Quantity：1setDimension：1M3Material：PE4.1.13.5.1Nutritionalagentblender（A-2874，Carbonsteellinedwithrubber）Model： KJB500Quantity：1unitMotorpower： 0.37KWRotationspeed： 136r/minLeafdiameter： 200mm4.1.13.5.2 Nutritionalagentmeasuringpump(P-2874)Quantity： 1setModel： GM0025Flow： 25L/hDeliverylift： 12barPower： 0.25kWManufacturer：ShanghaiHansheng4.1.13.5.3 Floatballlevelmeter(LSA2874V)Model： MAC-3Quantity： 1unitManufacturer： DalianMAC4.1.13.6H2SO4slot(V-2875)Quantity：1setDimension：1M3Material：PE4.1.13.6.1 H2SO4measuringpump(P-2875)Quantity： 1setModel： GM0025Flow： 25L/hDeliverylift： 10barPower： 0.25kWManufacturer：ShanghaiHansheng4.1.13.6.2 Floatballlevelmeter(LSA2875V)Model： MAC-3Quantity： 1unitManufacturer： Dal