建投vs麥克菲-4mw制氫裝置及相關服務采購附件部分

附件1：標的物交付時間表及對應職1部分的范1部分的范買方 辛營村，076561注所有均依照國際貿易術語INCOTERMS2010。2境分的范圍DAP附件2：供貨范圍和界制氫裝置交付部分分為三個批次，單一批次的單獨訂單不可行。批次1－3的組合對于裝八臺高壓高動力高效能的“alkaline2.0”制氫電解槽（高壓反應組裝，催化電極、薄膜。2:“麥克適用風廠輸入DCS”總體DCS(分散控制系統(tǒng))，用于快速回應控制波動的電力輸入、3:MCC架構和電氣連接至流程工藝部件、控制和附屬單元（接:2010076561賣方在此范圍項下將在制氫裝置（境分）建設施工階段：2的詳細設計正確地按功能整合;河北建投新能源在此范圍項下將在制氫裝置（境分）建設施工階段：與麥克能源提供聯(lián)合現(xiàn)場管理并人力資源； 附件3：技術協(xié)GUYUANWindHybridPowerPlantProjectPhaseI-HydrogenPlant沽源綜合能源站風電制氫項目一ANNEX3TECHNICALAGREEMENTINTRODUCTION簡 EXPERIENCESANDREFERENCES經驗及業(yè) PHASEISCOPEDEFINITION一期項目范圍定 OVERALLPLANTDESIGNFORGUYUANWIND-HYDROGENPOWERPROJECT沽源綜合能源站項目總體設 HYDROGENPLANTPHASEI氫能源站I TECHNICALEQUIPMENTILLUSTRATIONANDSPECIFICATIONS技術參 MCLYZERHYDROGENPRODUCTIONPLANTMCLYZER制氫 UTILITIESANDEQUIPMENT公用介質和設 TECHNICALDATAOFMCLYZER4MWHYDROGENPLANTMCLYER4MW制氫站技術參 APPLIEDCODESANDSTANDARDS采用標準與規(guī) TECHNICALANNEX技術附 P&IDMCLYZER400-30MCLYZER400-30P&ID P&IDPURIFICATIONANDDRYING純化和干燥P&ID P&IDMCLYZER400-30COMPONENTSDESCRIPTION MAINEQUIPMENTLIST主要設備 27GENERALPLANTLAYOUT工廠總體布 IntroductionMcPhyEnergyisaleadingEuropeandeveloper,manufacturerandintegratorofequipmentforhydrogenbasedenergysystems.McPhyEnergydevelops,manufactures,constructsandintegratesownandthirdpartytechnicalequipmentandcomponentstocreatesolutionsforthesupplyofhydrogenforindustrialapplication,mobilityandfortheconversionofelectricalintochemicalenergyforenergystorageapplications.Withmultiplereferences,McPhyhasdemonstratedbothitssuperiortechnologyforwaterelectrolysisandsolidstatehydrogenstorage,anditscompetencesandexperiencesinthedesignandbuildinthefieldofcomplexhydrogenhybridplants.McPhyhasdeliveredonaglobalbasenotonlytechnicalequipmentbutalsoturnkeyplantsuptomultiMWinstalledcapacity.麥克能源是歐洲氫能系統(tǒng)設備的開發(fā)制造和集成商。麥克能源開發(fā)制造，及建造和集成自己與第的技術設備和部件創(chuàng)造工業(yè)氫氣應用，以及移動和電能轉換為化學能的能源應用的解決方案。通過多個業(yè)ThecoreofthistechnicalproposalisMcPhy'sproprietaryandinnovative"Alcaline2.0"McLyzerwaterelectrolysistechnology,whichproduceshydrogenandoxygenthroughanelectrochemicalreactionpoweredbyelectriccurrent.ThehighlyefficientMcLyzersystemsarecharacterizedbyamaturedandrugged,butinnovativedesign,highoperationalsecurity,simplehandlingandlongdurability.McPhy'sadvancedelectrolyzertechnologystemsfromsustainableexperienceandknowledgelevelsinthehydrogenmarket.該項目的技術是麥克擁有的創(chuàng)新性的”堿性2.0”McLyzer,水電解制氫用,并且創(chuàng)新設備的特性,高運行安全性,操作簡單且使用長.麥克先進的電解技術源于長期在McPhyMcLyzersystemsandplantsmeettheinternationalstandardsCEandTüV，andthesystemsandplantsshouldmeetoroverstepthestandardsinChina.麥克McLyzer電解水系統(tǒng)以及工廠設備滿際標準如CE和TüV，同時滿足或高于中民共Electrolysissystemsareavailablewithdifferentperformancelevels.OurMcLyzersystemscanproduce100Nm3/hto400Nm3/hofhydrogen,whichequates0.5to2MWpowerinput.Aumoffourgeneratingunits(stacks)canbeusedperelectrolysismodule.Themodulescanbeinstalledeitherinso-called"skids"inanexistinginfrastructure,orfreestandingwithappropriatehousing(containerconstruction).電解系統(tǒng)可提供不同的產能水平,我們的McLyzer系統(tǒng)可生產100Nm3/h到400Nm3/h的制氫量.0.52MW輸入功率.4個制氫單元(電解槽),模Ifmorecapacityisrequired,oursystemscanbeexpandedto>500Nm3/hofhydrogenproduction.Itsmodulardesignmakesasubsequentextensionpossibleatanytimeandensuresacustomer-optimizedintegrationintoexistingsystemarchitectures.如產能要求更大,我們的系統(tǒng)可擴展到位>500Nm3/h的ExperiencesandReferencesMcPhyEnergy’sexpertiseliesinthedevelopment,constructionandinstallationofmanyinnovativeelectrolysersandturnkeyhydrogenplantsinthelast18years.Ourwell-foundedcompetenceisbasedonnumerousoperationalexperiencesinvariousindustrial,powerengineering,energyandpowertogasapplications.Ourstaffgaineditsknow-howinvariousrenownedcompaniesintheelectrolysis-and站交工程.我們的能力源于良好的基礎以及眾多的運行經驗和不同的工業(yè)應用,電力工程,能源Theproductioncapacityofourelectrolyserplantsvariesfrom1Nm3toseveralhundredsNm3ofhydrogenperhour.Duetotheirmodulardesign,theplantscanbeextendedandarefreelyscalable.我1立方米/小時到數百立方米/Mostimportantly,McPhyEnergy’selectrolysistechnologyhasbeendevelopedsuitedanptedforpowertogasapplicationfromrenewablewind-powergenerationforHECICNewEnergyfromMcPhyEnergy’sexpertiseandexperienceastheelectrolysistechnologyrformajorflagshippowertogasprojectsinEurope,includingtheflagshipprojectinBerlin–H2BER,andinPrenzlauinBradenberg,Germany,tonameafew.最重要的是，麥克能源的電解技術開發(fā)適用于再生風能進行電解氫的應H2BER，和德國BradenbergPrenzlau項目。PhaseIScopeDefinitionThissectionissuitedforPhaseIscopedefinitionandillustrationpurpose,forcommercialscopeofsupplypurpose,refertoCommercialPartAnnexIIIScopeofSupplyandBatteryLimits.該部份適用于OverallplantdesignforGUYUANWind-HydrogenHybridPowerproject沽源綜合能源站項目總體設計Basedonthefeasibilitystudysubmittedin2014,ahybridpowerplantshallbeinstalled,convertingexcesswindenergyintovaluablehydrogenenergy.TheoverallHydrogenHybridPowerPlantprojectwillbespiltintofollowingmainconstructionGUYUANWindFieldforgenerationofrenewableelectricpower(notscopeofthisproposal)HydrogenPlantforconversionofwindpowerintoPhase Construction:4MWCapacity1期項目建設:4MWPhase Construction:10MWExtension(plus6MW)atalaterstageFigure1:10MWHybridPowerHydrogenHybridUtilizationEquipment(notscopeofthisproposal;notyethydrogenstorageI (conventionalcompression)氫氣1期(傳統(tǒng)的壓hydrogenstorageII(innovativeMcPhysolidstatestorage氫氣2期(創(chuàng)新型的麥克固態(tài)儲氫技術hydrogentransportationhydrogenutilizationequipmentforfuel-cellvehicles用于電池汽車的hydrogenbasedelectricityHydrogenPlantPhaseI氫能源站IInPhaseI,4MWofhydrogenproductionsystemcapacitywillbeinstalledtoproducenominal800Nm3(nominalload)ofhydrogenperhour(20-135%bandwidth).Thetechnicallayoutforthebuildingisdesignedtohost10MW,butthescopeofthisproposalisforthefirststagePhaseI.TheplantisthecoreelementoftheoverallHydrogenHybridPowerPlantandwillconsistof:14MW的氫氣生產系統(tǒng),800Nm3/h額定負荷),（20-135%的調節(jié)幅度）,BuildingfortheHydrogenPlantPhaseIandII)氫能源站的主建筑物(1designedforatotalcapacityof10MWinstalledhydrogengenerators設MainInterfacesforHydrogenPlantMediaSupply(PhaseIand綜合能源站介質供應的主接口（1期和2期項目electricalpowerfrom35kVlinefedbyGUYUANwindfield電力由沽源風場otherconsumablesforhydrogenplantHydrogenGeneratorandAuxiliariesfor4MWPhaseI)4MW的制氫Transformer/RectifierStations(from35kVtransformerfeed)變壓器/整WaterPurificationUnits(fromundergroundwaterfeed)水凈化裝置(由地InstrumentAirsupplyNitrogenSupplyHydrogenGeneratorstacksHydrogenGeneratorProcessingStationsHydrogenPurificationSystemCoolingOverallControlsDCSHMI總體控制HydrogenOutputInterface(tohydrogenutilizationsystem)氫氣輸出接HCIGmeansHECICNewTechnicalEquipmentIllustrationandSpecifications技術設備說McLyzerHydrogenProductionPlant1McLyzerElectrolyzermodules電解槽模1Thecoretechnologytoproducehydrogen,consistingoftwoMcLyzer400-30modules,onpreassembledskids,deliveredfromMcPhyEurope.TheMcLyzer4MWproductionplantconsistsoftwoMcLyzer400-30.Eachelectrolyzerconsistsessentiallyof:Celldesignwithminimaldistancebetweenelectrodesanddiaphragm電極Endelectrodes,oneactingasanodeandtheotherasacathode,bothprovidedwithelectricityconnectionlugs尾電極,一端擔當陽極,而另一端擔當陰CellframeMetallicbipolarplatesAsbestos-freediaphragms,separatinganodicandcathodicSealsofasbestos-freematerialforthecellblocksealing電解槽采用非石棉密Pressandsupportingstructurewithpressureplates,tierodswithnuts,pressurewashers,isolationbushings采用壓板支撐結構,壓緊螺桿和螺帽,壓力Gas/electrolyteseparators氣體/CirculationpumpfortheelectrolyteDeminwaterpumpHeatexchangerfortheelectrolytecircuitGascoolersforhydrogenandoxygenValvesandpipesforinternalconnections連接的管道及閥AllelectrolyzermodulecomponentsareassembledandmountedonasupportingskidThesetupsystemisdefinedasHazardousZone2.Transformer-/rectifierandcontrolequipmentareplacedinaseparateroombuilding/containerinanon-hazardousarea.所有電解槽模塊的部件裝配在支撐框架上,該系統(tǒng)2級防爆區(qū),變壓器/整流器和控制設備,安裝在單獨的房間(廠房/集裝箱)為非防爆區(qū).Figure2:McLyzer400-30Indicativepicture,subjecttochangeofinterfaceandarrangement圖2:McLyzer400-30指示可能變化接口以及布置方:reachapermanentperformanceof100ofitsnominaldefinedproductionprovidethetotalgascapacityinpermanentoperation,evenincasetheactivatedelectrodesarecompleydegraded.保證提供其總產氫能力能運行,Transformer/rectifierfortheelectrolysissystem電解系統(tǒng)的變壓器／整流Thetransformer/rectifierunitconvertstheexistingACsupply(mediumvoltagelevel,35kV)totheDCvoltagesupplyrequiredbytheelectrolyserstack.變壓器/整流器裝置把提供的交流的電能(中Inaddition,therectifieroffersthepossibilityofoperatingtheelectrolyserwithinaloadrangeof25to133%ofthereferencenominalpower.并且,25133%的標Nom.inputvoltage[VAC 192Outputvoltage[V; Conformity IEC62103Auxiliaryvoltage(Fuse16A,Load1A):230/400Main 47to63Circuit Thyristorphaseangle,電路原理 可控硅相位變Basic Watercooledpower基本電路 水冷電源模 RAL >Cos >0,9@20%..DimensionMaster 1200x600x2200(LxBxWeightMaster- ca.DimensionSlave 1200x600x2200(LxBxWeightSlave- ca.Thetransformer/rectifierunitsfortheMcLyzer4MWplantconsistMcLyzer4MW變壓器/整流器單元包括2unitsof3-phasecastresintransformer2rectifierTHYROBOXTMHC,eachconsistingof1mastercabinet+7slave2臺THYROBOXTMHC，整流器，每臺包括1個主屏和7Operatingelementsanddisplaysincabinetdoor(touchOutputcurrentOutputvoltageInterruptionsrectifier(signallamps,collectiveHandcontrolsforlocalHardwareOutput:potential-freecontact230VAC:emergencyswitchInput:potential-freecontact230VAC:emergencyswitchfromRemotecontrolviaprofibus控制,可通過profibusAuxiliaryequipmentlikecontactorcoils,motorprotectioncircuitbreakers,auxiliaryrelay,overloadrelay,controlsystemforautomaticconstantcurrentcontrol.Themodulesformingtherectifiersystemarewiredandmounted,readyforoperation.Thesupplylimitisthetransformer’sprimaryconnectingterminal.PowercablesandDClinkbarstotheelectrolyzerstacksareincluded.Purificationanddryingunit純化和干燥裝Toachieveitsspecifiedquality,adryingsystemisusedforcleaninganddryingthegas.Theunitisdesignedforanabsoluteflowrateof1.300Nm3/handanoperatingpressureupto31bar.Theplantincludesareactorwithnoblemetalcatalystfillingandtwodryerswithmolecularsievedryerandautomaticregeneration.1300Nm3/h，31bar12個填充分子篩的干燥塔，并且自動ThepurificationanddryingunitworkswithoutanyH2lossesduetoitsinnovativeprocessdesign.純化Purificationanddryingprocessdescription純化和干燥工藝流程描(ReadinconjunctionwithTechnicalAnnexP&IDinSection6)(同時參閱6PID圖)Thequotedhydrogenpurificationanddryingunitmainlyconsistsofonereactorfilledwithapalladiumcatalystandtwoadsorbersfilledwithmolecularsieves.氫氣純化干燥裝置主要包括1個鈀催化劑的純2臺填充分子篩的吸附干燥塔.Atfirst,thehydrogentobepurifiedanddriedpassesthereactorthatisfilledwithapalladiumcatalyst,wheretheoxygenreactswithhydrogenatthecatalystproducingwater.Beforethehydrogenentersthereactor,itisheateduptoapproximay10°Cabovethedewpointtopreventeventualcondensationofthewatercontainedinthegas.Sincethereactionisexothermic,thepurifiedhydrogeniscooleddownstreamthereactorbymeansoftwoheatexchangersconnectedinseriesbeforeenteringthedryingunit:thefirstheatexchangerutilizescoolingwaterascoolingmedium,whilethesecondoneutilizeschilledwater.Additionally,thesecondheatexchangerisequippedwithanintegratedseparatortoremoveanyremainingdroplets.首先,氫氣通過填充有鈀催化劑的反應器進行純化處理,氫氣在催化劑的作用下于氧氣生成水,氫氣在進入反應器之前首先進行加熱,加熱溫度超過溫度10度左右,燥系統(tǒng).第1個換熱器用冷卻水作為冷卻介質,第2個換熱器用冷凍水作為冷卻介質.并且,第2個換熱Thedryingunitconsistsoftwoverticaladsorbers,workingfullyautomatically,oneinoperationandoneinregenerationmodetomaintainacontinuousprocessflow.Thehydrogen(wet)isdirectedtothebottomoftheadsorber,whichisinadsorptionmode.Byflowingupwardsthroughtheadsorptionbedthewaterdewpointisreduceddowntospecifiedvalues.Finally,thehydrogendry)isdischargedatthetopoftheadsorberandfedintocustomer’ssystemafterpassingafilterinstalleddownstreamtheunit,whichremoveseventualresidualparticlesoftheadsorbentagent.氫氣(濕的)直接由吸附器的底部進入,然后進行吸附.通過吸附床的吸附,其含水的降低到規(guī)定的Thesecondadsorber,whichhaspreviouslybeenoperatedinadsorptionmodeanditissaturatedwithwater,isinregenerationmode,whichconsistsoftwophases:desorptionandcooling.Thedesorption(heating)occursincounterflowtotheadsorption,whilethecoolingprocessiscarriedoutinparallelflowtotheadsorption.，Apartialstreamtappedofffromthewetgasisutilizedasregenerationgas.Thisisdonebymeansofacontrolvalvelocatedupstreamtheabsorbers,whichisinthethrottlingposition.Thispartialstreamisheateduptotherequiredregenerationtemperatureviaanelectricalheaterandcirculatedtothetopofthesecondadsorber,currentlyinregenerationmode.Byconveyingthishotgasdownwardsthroughtheadsorberbed,theadsorbentisregenerated(desorptionoractivationphase).Afterleavingtheadsorber,thepartialstreamiscooledinacoolingwaterheatexchanger,equippedwithanintegratedseparatorforremovalofcondensate.Subsequentlythecooledregenerationgasismixedwiththemainstreamagaindownstreamthethrottlevalve.節(jié)流的氣流2,向下輸送熱氣體進行吸附劑再生去吸附過程).離開吸附床后的氣體通過水冷換熱器進行冷卻,換熱.Aftertheactivationphasehasbeencompleted,theadsorptionagentiscooledsothatnosurgesinmoistureortemperatureoccurwhentheadsorberischangedover.Duringthecoolingphase,thepartialstreamistappedoffupstreamtheelectricalheater,whichhasbeenswitched-off,andcirculatedtothebottomoftheadsorbers.Thepartialstreamisconveyedupwardsthebed,coolingdowntheadsorbentbacktooperatingtemperatures.Afterleavingtheadsorber,thecoolingpartialstreamisalsorecooledandthenmixedwiththemainstreamdownstreamthethrottlevalve.在再生過程完成后,吸附劑進行TheregenerationoftheadsorberiscompletedwhenthecoolingphaseisFigure3:PurificationanddryingunitindicativeProcesscontrolandsecuritysystems工藝控制和安全系Monitoringandsignalsystem:監(jiān)測和信號系統(tǒng)Allsystemcomponentsoftheelectrolyzerplantarecontrolledandmonitoredbyacentralprocesscontrolsystem.Inalarmsituations,theaffectedsystemswillbebroughtintoasafestate(FailSafe).Therefore,theMcLyzermodulesneedtobeintegratedintoasuperordinateprocesscontrolsystemtoguaranteeaproperfunctionalityofthemainsystemitself.Atechnicalstandardsolutionforsuperordinatecontrolsystemsisthesolution“ProcessControlSystem7”(PCS7)providedbythecompanyAG.Thissolutionoffersthefollowingfunctionalities:電解制氫站整個系統(tǒng)的監(jiān)測和控制都通過工藝控制系統(tǒng)進行控制.在狀態(tài),受影響的系統(tǒng)將進入到安全狀態(tài)(故障保護),因此,McLyzer模塊需要集成到工藝控制系統(tǒng),確保適當的功能性.上CentralsystemSupportofdifferentcommunicationModulebasedintegrationofsystempartsandthereforeeasilyAwideareaofprocessautomationSupportofindustrialsafetyConsiderableprocessvisualizationIntegratedenergyApossibilitytoarchiveandevaluateorprovideprocessFigure4:Exampleformonitoringsystemindicativepictureof圖4:系統(tǒng)實例Figure5:Secondexampleformonitoringsystemindicativepictureof圖5:系統(tǒng)實例PCS7providesdifferentsystemarchitectureswhichmainlydiffersincasesofdatasafety,dataaccessibilityanduseraccessibility.PCS7提供不同的系統(tǒng)架構,其主要不同之處是數據的安全,數據的存取以及用戶獲得數據的容易性.Systemdescription:系統(tǒng)描述:ThefollowingfigureshowsapossiblePCS7-configurationfortheelectrolysisplantwithouttechnicaldetails.ThereareotherconfigurationsavailablewhichdependsontheclaimedscaleofUsedtooperatetheUsedtooperatethesystemv visualizationprovidedbythebothOS-ServersOS-TERMINALTERMINALEngineering

OS-Server

OS-ServerPLANTPLANTUsedfortheprocesshandlingandfortheintegrationofthePCS7-DecentralPeriphalUnitsforeach10MWCOM-PCS7-DecentralPeriphalPCS7-DecentralPeriphalUnitfortheofthefieldbus-unitsofeach10MWFIELDFieldbus-Figure6:PossiblePCS7Hardandsoftwareequipmentformanualandautomaticshutdownareincludedinthesupply.請補充翻譯供貨中包括手動和自動停機的硬件以及軟件設備，同時麥克將開放控制系統(tǒng)及接口，以便制氫系統(tǒng)與風電場SCADA系統(tǒng)實現(xiàn)對接與整合。Instrumentation儀Forthereliableandlargelyautomaticoperationmonitoring,followinginstruments/sensorsare為實現(xiàn)可靠和大量的自動運行和監(jiān)測,采用有下列儀表和傳感器ElectricityBlockclampSystemElectrolyevelindicatorandautomaticlevelcontrolinthegasAutomaticcontroloffeedwaterDisplayandcontrolofelectrolyte-andgasAutomaticmeasurementsofhydrogen-andoxygen-qualitydownstreamAutomaticmeasurementsofhydrogenqualitydownstreampurificationanddryingunit(humidityandO2inH2).UtilitiesandEquipmentPotassiumhydroxidesolutionKOH)氫氧化鉀溶液Fortheelectrolyzer-startup12,4m3ofpotassiumhydroxidesolution(KOH,28%,chemicallypure,low-chlorinequality)isneeded.Itwillbeusedtoactivatethesystemaftertheinitialfilling,andshallbereplacedafteractivationwithnewKOH.Therefore,awholeamountof24,8m3KOHareneededfortheinitialstartup.12.4m3的氫氧化鉀溶液(KOH,28%的濃度化學純低氯品質),用該溶液進行首次充裝和活化,KOH溶液,因此,24,8m3Electrolytestation電解液Theelectrolytestationisnecessarytoensureasecurehandlingwithpotassiumsolutionincompliancewithapplicableenvironmentalprotectionrequirements.Followingfunctionshavetobeguaranteed:系統(tǒng)需要設置電解液站,以確保滿足環(huán)境保護的求以及處理氫氧化鉀的溶液.保證實現(xiàn)下列功能Alkalinestoragereservoirhastobefilledwithpotassiumsolutionfromanexternalreservoir.EmptyingthealkalinestoragereservoirinaproperexternalFillingtheelectrolyzermodulewithpotassiumsolutionfromthealkalinestoragereservoir.Emptyingthepotassiumsolutionfromtheelectrolyserinthealkalinestoragereservoir.電解槽的堿液清空排放到堿液容Skimminganyliquidsfromtheelectrolyser’ssump(leakage)intothealkalinestoragereservoir(triggeredbyemptyingtheleakyelectrolyser,e.g.duelevelalarm).位)Feedingofconcentratedpotassiumsolutiontoincreasetheconcentrationinthereservoirandpumtheelectrolytethroughthedrainfiltertomixitintheelectrolyserandcleanitmechanically.集中把氫氧化鉀溶液泵入到堿液容器進行提高濃度并經過過濾器對溶液進行機械Replenishmentofwatertodecreasetheconcentrationinthewatertreatmentplant.eelectlytesatincositsof6electlytectaierithatesadcnectigpiesrtasimsltin.Italsohasliqidlevelgage.Tecaacityofthecaierissficiettoasrbteentieelectolytetyofteelectolyerouleus>13eseve.電解液站包括6個堿液容器.以及相應的氫氧化鉀溶液連接管道同時配有液位指示計容器的溶量滿足所有電解槽模塊電解堿液的總量再加大于3的安全容積。1electrolytecontainer1個電解液容器Workingpressure:工作壓力:DetailedpartsandcomponentsreferstolayoutitemClosedloopcoolingsystem閉路循環(huán)冷卻系Theexcessheatgeneratedduringtheelectrolysisprocesswillbeevacuatedfromtheelectrolyteandthegasesthroughseparatedheatexchangingsystemswhichareintegratedintotheelectrolyzermodule.Forthispurpose,anexternalcoolingsystemisused,consistingofacompressorchillercombinedwithadrycooler.電解過程中產生的額外熱量將分別通過電堿液換熱器和氣體換熱器進行轉移,換熱器全部集Feedwatertreatmentfordemineralizedwater)補給水處理（用于水脫鹽Theelectrolyzerstacksrequireahigh-qualitydemineralizedwatersupply.Forthisreason,ademineralizingwatertreatmentisnecessary.Theuntreatedprimarywaterhastohaveapotablewaterquality,freeofmechanicalimpuritiesandfreeofsignificantconcentrationsofiron,manganeseandchlorine.電解槽要求高品質的脫鹽水供應,因此,需設置脫鹽水處理系統(tǒng).系統(tǒng)的原水供給需達到飲Todemineralizethewater,areverseosmosissystemwithmembraneprocesseswillbeused.Adownstreamionexchangerensureshighfeedwaterquality.脫鹽水處理將采用反滲透立子交換膜法.在下游設有離子交換器,確保高品質的補給水ForForthefinaldesignofthedeminwaterplant,acompletetapwater ysisisneededandhastoprovidedbythecustomer.最終完成脫鹽水處理站的設計,需要用戶提供詳細的自來水分（本項目方案應為水凈化后電解）Nitrogensupply氮氣供Forasecurestart-upandshutdownoftheelectrolysisplant,acompleteinertizationofthosecomponentsthatcouldcontainhydrogenoroxygenisnecessary.為安全的啟動及停運電解制氫站,AnappropriateN2supplyisinaccordancetothefollowingrequirements:適當的氮氣供應依據下列N2-consumptionforstart- ca.39kg(inertizationH2-啟動氮氣耗量 約39kg(氫側惰性化處理N2-consumptionfor ca.80kgshutdown,H2-andO2-停運氮氣耗量 約80kg,氫側和氧側惰性化處Required O2< <濕度 <0,1mg/m3and顆粒物TechnicalDataofMcLyzer4MWHydrogenProductionPlantMcLyer4MW制氫站技術參數BelowindicativetechnicaldataofMcLyzer4MWHydrogenMcLyzer4MWTechnicalRequirementsand格Comments4MWElectrolyzersystem4MWH2productioncapacity@100nominalload<InstalledPowerAmounectrolyzerModules電解槽模塊數2Ex-Zone防爆 deoxo/dryer)工藝部分電解槽AvailabilityperannumEnergyconsumption@operationalconditionsSpec.Energyconsumptionstack(DC)電解槽直4,425+/-1styearoperation1年運行，Spec.EnergyconsumptionElectrolyzerModules(AC),nominalload電解槽模塊交流電耗,額定4,680+/- 電解槽,變壓器/整流器,泵,控制系RequirementcoolingconsumptionelectrolyteTein=20°C,@umRequirementcoolingconsumptiongas氣體冷卻@20°Cinletcoolingwatertemperature冷卻水進口溫度為Spec.EnergyconsumptionElectrolyzerStandby電解槽備用狀態(tài)交流能controlsystem控制系Dimensionelectrolyzermodule(LxBxH)電12,4x3,3xpermodule(2modules每個模塊(總共為2個模塊OverallDimensionHydrogenplant(LxBxH)制30x56xsee“Annex6PlantLayout10MWhybridpowerplantHECICNEWENERGY”fromfeasibilitystudy附件610MW綜合能源站布置Weightinclmedia)重GasqualityO2inH299,6+/-DownstreamElectrolyzerH2inO299,4+/- moduleKOHinH2氫氣中KOHDownstreamdeoxo/drier@i30°Cand31baraoperationpressure脫氧干燥器出口運行壓力31H2OinH2StackvoltageDC)<@Concentration濃Amountofelectrolytesystem總2ModulesMclyzer400-302Mclyzer400-30模Stockofelectrolyte(Electrolytestation)0LifetimePlanttotalStackyearstooverhaul大7toundernormaloperationDegradation降abt.15todegradationinaverage平均降率Ambienttemperature環(huán)境溫-25°C-+5°C-Altitudemagainst<AuxiliarycomponentsQualitydeminWater<Abouttoassignregardingtechnicalsolution(reverseosmosissystemabout50%losses)依據技術解決方案(反滲透系統(tǒng)的損失量約ConsumptiondeminWaterincl.lossesofcondensateinandO2包括氫氧中損Installedpower regardingsolutionspecEnergyconsumption特定能量消<wareparts易耗About regardingsolution依據技術解決方Pressureinterfaceinlet3Dimensions尺(LxBx regardingsolution依據技術解決方Weight重 regardingsolution依據技術解決方CoolingsystemCoolingpowerrequirementPressureinletinterface<Coolingwatertemperatureelectrolyte卻水溫CoolingwatertemperaturegasInstalledpowerdrycoolerInstalledpowerchilleronlyneededabove15°Ccoolingwatertemperature15°CSpec.Energyconsumptionmin.消Spec.Energyconsumptionmax.消hotambienttemperature環(huán)境度Dimensions尺(LxBx regardingsolutionWeight重 regardingsolutionNitrogensupply (commissioning)每次吹掃耗量(調式purgingH2-andO2-site氫側和 missioning)每次吹掃耗量(停運purgingH2-andO2-site氫側和RequiredgasqualityO2<residualhumidity<0,1mg/m3undPressureInterfaceinlet接口壓[bar6..InstrumentairsupplyConsumptionnormaloperation<ConsumptionStart/Stop啟運/停運消耗< abt.15sec.典型啟動過程15Pressureinterfaceinlet[bar9–Quality品Dry干Dewpoint=-25°C-Transformer/rectifier變壓器/12-Pulsewatercooledrectifier12脈沖冷Thyristor可控硅Amountperunit)數量(每臺4InstalledpowerVoltageoutputDCValcurrentDCACoolingwaterrequirement冷卻水要ClosedloopcoolingEfficiency效%CosPhi余@20%..100%Dimensionspower/controlcabinetLxBx1,2x0,6xDimensionschoppercabinetLxBx1,6x0,6xType/Principletransformer型號/變壓形Dry干Amountperunit1Dimensionstransformerbox變壓寸LxBx2,9x3,4xpertransformer器6pertransformer器ElectrolytestationTypeprinciple型號/形Description描Storagecapacity容Proposedfor10MW10MW源站提Operationpressure運行壓Dimensions尺LxBx technicalsolution依據Weightempty重 technicalsolution依據Typeprinciple型號/形Description描heatregeneratingAmountofunits裝置數1Media介Hydrogen氫Rangeofoperation%30..ImpuritiesinletO2進口殘留氧含Vol<Capacity產Operationpressure運行壓[barInlettemperaturemax.Inletmoisture進口濕[gSaturated飽abtResidualmoistureunderDP- pressureOutletgastemperatureca.產品氫 ≥-Controlpower控制電230V,50Power動力電400V,5015°C,3Instrumentairinlet5barg,DP-Coolingwaterrequirement冷卻水要InstalledpowerEnergyconsumptionConsumptionH2(activation,cooling)4Dimensionsperunit裝置尺LxBx3.500x2.000xWeight重Ex-ZoneOperationoftheelectrolysissystemStart-uptime(coldstart)tonormaloperationconditions啟運時間(能啟動)ca.Startfrommin.Shutdown(normalSTOPfromnominalload)停機(從額定負荷正機 requirementfromMintoNom<From30%to.60–Max./min.operationpressure最大/最運行壓[bar25-flexibleadjustmentoperationpressureProcesscontrolandsafetysystemsDescriptionofthecontrol&safetyS-7/PCS-Allthecomponentsrelatedtotheelectrolysismoduleswillbecontrolledandsupervisedbyacentralizedprocesscontrolsystem.Incaseofanalarmsituation,thissamecontrolsystemwillsettherespectivecomponentsintoasafetymode(“Fall件,都由控制系統(tǒng)進行控制和監(jiān)測如出現(xiàn)警情況該控制系統(tǒng)將西門子Thehardwarecomponentsandsoftwareproceduresforthemanualand shut-offofthesystemarealsoincludedinthisscopeofsupply.運行控制的硬件及軟件Theprocesscontrolsystemofthewholeelectrolyzerwillbelocatedinacentralcontrolroomlocatedon統(tǒng)將安裝在現(xiàn)場的控制室Theprocesscontrolsystemconsistsintwomutuallyindependentcontrolloops:工藝控制系統(tǒng)包括2工藝控Safety-orientedshutoffs,inducingasafeplant安全停車包括工廠安條IntegrationcontrolsystemofelectrolyzerintoSCADAsys.SCADA系Basissoftware基礎軟GcessDataexchangeprotocol協(xié)議Ethernet“(PROFINET,61158/61784)orQuality,Health,environment,safety(HES)andcertification質量健康環(huán)境安全> measures施Emissions排Excl.ProducedgasesH2andO2Noiseemissions噪ca.62±2Acc.DINENISOMonitoringgasquality(H2inO2andO2inMethods/Downstreamel