IC厌氧反应器多层旋流布水与重渣排放系统研究王建光

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2016-05-062016-08-13514753152014-Z-Y092014-GX-2191987-E-mailpeterjgwang@163.comE-mailchenzailiang@suda.edu.cnIC215021ICUASBIC。。。IC。IC。ICS216.4B1000-1166201703-0056-06MultilayeredCycloneWaterDistributionandHeavySludgeDischargeSystemforICAnaerobicReactor/WANGJian-guangCHENZai-liang/SchoolofMechanicalandElectricEngineeringSuzhouUniversitySuzhou215021ChinaAbstractInviewofthemainstructureproblemsexistinginICanaerobicreactor’swaterdistributionsystemandthetrou-bleofreactorcalcificationthisarticlefocusedonoptimizationdesignforthestructureofwaterdistributionsystemonthebasisofcomparisonandanalysisofUASBandICtypicallayout.Amultilayeredcyclonewaterdistributionandheavysludgedischargesystemwasproposedwhichwascomposedofmulti-layerwaterdistributionpipeandinvertedconeflowguideplate.Throughhydrauliccalculationofthesystemandmotionanalysisofbiologicalsludgeandheavysludgeitwasfoundthattheuniformityofwaterdistributionwasimprovedavoidedwaterdistributiondeadzoneachievedtheseparationofheavysludgefrombiologicalsludgeandenhancedthemixingdegreeofwastewaterorganicswithgranularsludge.Thisef-fectivelystrengthenedthemasstransferandreactionprocess.FinallythisarticleprovidedanempiricalanalysisbasedonamodifiedICreactorproject.Theoperationdataandinfraredthermographydetectionshowedthatthemodifiedschemea-chievedexpectedeffect.Hencethisprovidedanewmethodforsolvingthecalcificationproblemscausedbywaterdistribu-tionandheavysludgedischargeforICanaerobicreactor.KeywordsICanaerobicreactorcyclonewaterdistributioninvertedconeflowguideplateheavysludgedischargesys-temICUASB。2080IC1。US-AB、、、2。。IC、、、、。UASB3。IC。65ChinaBiogas20173534。。。。1UASBIC5。UASB1。6。UASB。UASB1。。、7。1UASBIC182。。。9。。。。2.布水器1.进水3.流化床反应室2IC、IC。。。。2IC110。2。。3。4、75ChinaBiogas2017353。3。3.13。倒锥形导流板布水管道3。11。。。50%12。IC。3.24。。。413。--14。。。3.3ICQ=πD2Vu41DmVum·h-1。d=10004Q3600πV槡D2NS=πD24N3rr=S槡π42d=10004Q3600NπV槡d5Qm3·h-1Vdm·s-1。QiQ1Qi-1m85ChinaBiogas2017353Q1=Q2Q2=Q1-Q2N=1-1NQ2Qi=1-mNQ2626did1=10004Q13600πV槡g=2Q3600πV槡gd2=10002QN-13600πVg槡Ndi=10002QN-m3600πVg槡N75。。。。罐壁倒锥形导流板活性污泥及沼气泡较低压区较低速旋流剪切混合区压差逆流较高压区转高速旋流5。、、。。。。6。。活性污泥重渣64ICФ12.5m×24m7。14824850cm。7IC8IC95ChinaBiogas2017353。。。。。。。。。。IC。1。1ICQ/m3·h-1982Vu/m·h-18Vd/m·s-11.1Vf/m·s-12.17。2m·s-1mmDNm·s-1d11.15624002.17d21.13974001.09d31.13243500.95d41.12292500.813。5。3Vf/m·s-12.1N/pcs18S/M26.824m·s-1mmDNm·s-12.195.8802.68COD≤3000mg·L-1COD≤900mg·L-1COD70%。COD30%IC65%。0.35~0.42kgCOD。IC86%。。15。IC9、16IC。10。。5。IC06ChinaBiogas201735321.5℃20151050-5-9.1Sp19ICSp110。IC。ICIC。1。。2。。3。。4。/。5。。6。。。1.ICJ.200117126-29.2.ICJ.2014412075-76.3WDriessenPYspeert.Anaerobictreatmentoflowme-diumandhighstrengtheffluentintheagro-industryJ.WaterScienceandTechnology1999408221-228.4.J.200223292-95.5AwadAbdelgad.、J.20143392244-2250.6GLettingaLWHulshoffPol.UASB-processdesignforvarioustypesofwastewatersJ.WaterScienceandTechnology199124887-107.7.J.2004342261-268.8.P.CN101193826A2006-06-04.9.J.200746z1225-226.10.UASBJ.2012281873-75.11.J.1995173109-110.12.J.2011222-3.13.--J.201037235-36.14.J.2015443580-582.15.J.200323124-28.16.J.2013262136-141.16ChinaBiogas2017353

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