进口潜水射流曝气机/Submersibleaerator/德国品质德国KAYSEN凯森进口潜水射流曝气机概述深水自吸式自耦式潜水射流曝气机是向曝气池内曝气的废水装置，是废水活性污泥法生物处理系统曝气装置的一种类型。由水泵将泥、水混合液打入射流曝气器喷嘴，并高速喷出，在射流曝气器内，氧转移过程的实现是在这个射流曝气器喷嘴周围使压缩空气（或空气直接吸入）与泥水混合液混合并在吼管中强烈搅动，气泡被粉碎成雾状，继而在扩散管中由于速头变成压头，微细气泡进一步被压缩，氧即迅速转移到混合液，从而强化了氧的转移过程，氧转移效率可提高到30-35%以上主要特点：●自重***，安装方便，可在不中断工艺运行的状态下自由布置●设计结构紧凑，利用自吸功能无需外接气源；●主机潜水作业减少占地面积，噪音小；●可直接在氧化塘中使用，节省基建成本；●***移动的曝气装置，曝气时兼有搅拌功能；●底盘可根据用户要求作特殊设计。主要优点：●采用潜水电***封技术的水下电机；●叶轮与电机直联，结构简单，效率高，寿命长；●可加网状进水口，避免***进入机体引起不必要的***；●可通过进气阀调节进气量；●除电机外，其它部件材质有不锈钢、碳钢和铸铁供选择。主要应用：潜水射流式曝气机用于各种污水处理工程中生化处理工艺的曝气池、曝气沉砂池、预曝气池、好氧硝化池曝气充氧混合及养殖塘增氧。潜水射流曝气机选型建议从五个方面加以考虑，既液体输送量、扬程、液体性质、管路布置以及操作运转条件等。1、流量是选射流曝气机的重要性能数据之一，它直接关系到整个装置的的生产能力和输送能力。如设计工艺能算出离心曝气机正常、较小、较大三种流量。选择离心曝气机时，以理想流量为依据，兼顾正常流量，在没有理想流量时，通常可取正常流量的1.1倍作为理想流量。2、扬程是选射流曝气机的又一重要性能数据，一般要用放大5%—10%余量后扬程来选型。3、液体性质，包括液体介质名称，物理性质，化学性质和其它性质，物理性质有温度c、密度d、粘度u，介质中固体颗粒直径和气体的含量等，这涉及到系统的扬程，有效气蚀余量计算和合适泵的类型：化学性质，主要指液体介质的化学腐蚀性和毒性，是选用泵材料和选用那一种轴封型式的重要依据。4、管路布置条件指的是送液高度送液距离送液走向，吸如侧较低液面，排出侧较高液面等一些数据和管道规格及其长度、材料、管件规格、数量等，以便进行系梳扬程计算和汽蚀余量的校核。5、操作条件的内容很多，如液体的操作T饱和蒸汽力P、吸入侧压力PS（***）、排出侧容器压力PZ、海拔高度、环境温度操作是间隙的还是连续的、泵的位置是固定的还是可移的。GermanyKAYSENImportedSubmersibleJetAeratorOverviewThedeepwaterself-primingself-coupledsubmersiblejetaeratorisatypeofwastewaterdevicethataeratestheaerationtankandisatypeofaerationdeviceforthebiologicalwastewatertreatmentsystemofthewastewateractivatedsludgeprocess.Themudandwatermixtureispumpedintothenozzleoftheincidentaeratorbyawaterpump,andissprayedatahighspeed.Inthejetaerator,theoxygentransferprocessisrealizedbydirectlyinhalingcompressedair(orair)aroundthenozzleofthejetaerator.Mixingwiththemuddywatermixtureandvigorouslystirringinthemanifold,thebubblesarepulverizedintoamist,andtheninthediffusiontube,thetipbecomesapressurehead,thefinebubblesarefurthercompressed,andtheoxygenisquicklytransferredtothemixture,therebystrengtheningOxygentransferprocess,oxygentransferefficiencycanbeincreasedto30-35%ormoremainfeature:●Self-repositioning,easytoinstall,freetoarrangewithoutinterruptingtheprocessoperation●Thedesigniscompact,andtheself-primingfunctiondoesnotrequireanexternalairsource;●Thehostdivingoperationreducesthefloorspaceandthenoiseis***all;●Itcanbeuseddirectlyinoxidationpondstos***einfrastructurecosts;●Independentlymovingaerationdevice,whichhasastirringfunctionwhenaeration;●Thechassiscanbespeciallydesignedaccordingtouserrequirements.Themainadvantage:●Underwatermotorwithsubmersiblemotorsealingtechnology;●Theimpellerandthemotoraredirectlyconnected,thestructureissimple,theefficiencyishigh,andtheservicelifeislong;●Itcanbeaddedwithameshinlettopreventforeignmatterfromenteringthebodyandcausingunnecessarydamage;●Theintakeairamountcanbeadjustedthroughtheintakevalve;●Inadditiontothemotor,otherpartsare***ailableinstainlesssteel,carbonsteelandcastiron.mainapplication:Thesubmersiblejetaeratorisusedintheaerationtank,aeratedgritchamber,pre-aerationtank,aerobicnitrificationtankaerationandoxygenationmixingandaquaculturepondoxygenationinvarioussewagetreatmentprojects.SubmersiblejetaeratorselectionItisrecommendedtoc***iderfiveaspects,suchasliquiddeliveryvolume,head,liquidproperties,pipinglayout,andoperatingconditi***.1.Flowrateisoneoftheimportantperformancedataoftheselectedjetaerator,whichisdirectlyrelatedtotheproductioncapacityandconveyingcapacityoftheentiredevice.Forexample,thedesignprocesscancalculatethenormal,***allandlargeflowratesofthecentrifugalaerator.Whenacentrifugalaeratorisselected,thenormalflowrateisbasedontheidealflowrate.Whenthereisnoidealflowrate,1.1timesthenormalflowratecanbetakenastheidealflowrate.2.Theliftisanotherimportantperformancedataofthejetaerator.Generally,itshouldbeselectedbyamplifyingtheliftby5%-10%.3,liquidproperties,includingliquidmedianame,physicalproperties,chemicalpropertiesandotherproperties,physicalpropertiesaretemperaturec,densityd,viscosityu,solidparticlediameterandgascontentinthemedium,etc.,whichinvolvestheliftofthesystem,effectiveCalculationofc***itationallowanceandtypeofsuitablepump:chemicalproperties,mainlyreferstothechemicalcorrosivenessandtoxicityoftheliquidmedium,whichisanimportantbasisforselectingthepumpmaterialandselectingthetypeofshaftseal.4.Pipelinelayoutconditi***refertotheliquidfeedingheight,theliquidfeedingdistance,thelowerliquidlevel,thehigherliquidlevelonthedischargeside,andotherdataandpipespecificati***andtheirlength,materials,pipefittingsspecificati***,quantity,etc.InordertocarryoutthecalculationofthecombingprocessandthecheckingoftheNPSH.5.Therearemanyoperatingconditi***,suchasliquidoperationTsaturatedsteamforceP,suctionsidepressurePS(absolute),dischargesidecontainerpressurePZ,altitude,ambienttemperatureoperationisgaporcontinuous,pumppositionisfixedStillremovable.)