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2015-12-142016-01-301991-15151230919810429523@qq.com。doi10.11988/ckyyb.20151045201734320-24PTA222000PTAPXPTA。TA。PTA、TA。。PTAPTA、-。、、、、PTA-+、+A/O、A/O。、NPMgFe、pHPTA。PTA。PTATAX703A1001-5485201703-0020-051PTAPTA。PTAPXPTA。2①PXCTA②CTAPTA1-2。PTATA、BA、、、。TA3。PTA①CODCODCOD4000~9000mg/LTA1000~2500mg/L800~1200mg/L②>45℃80~90℃③pH5~11213④、1-4⑤TA5。PTA、6。2PTA2.171。。17Fig.1Aerobicdegradationprocessofaromatichydrocarbons785PTA16SrDNA5、、、、PTA524hPTA76.5%75.3%75.7%81.9%81.6%。PTAPTAPTA。2.2343Vol.34No.320173JournalofYangtzeRiverScientificResearchInstituteMar.2017。CH4CO2。BA2。2BA7Fig.2AnaerobicdegradationprocessofBA7BACH4CO2。、、、。2.3TAG.Engelhardt9TA。10TA2①②BABA。11-70%TADO>5mg/LTA97%。D.W.Ribbons12、。132TATA。14TA15∶120mL/min10h。3PTAPTA。3.1。CODCheng15UASBCOD1.82kg/m3·d62%。Fa-jardo161997。JiYoungKim17UASBPTApTOLBATApTOLUASBCOD4.18kg/m3·d>99%pTOL1.35kg/m3·d>99%SEMFISH。PTA、、。。3.22+2PTA18。1.5~2kgCOD/m3·dCOD0.2~0.3kgCOD/m3·d。2CODTACODcr4000~9000mg/L100mg/L。2、、、。219、DO6~8mg/L。20MBR+CSTRPTA。MBRPTATAMBR3~10kgCODCr/m3·dCODCrCODCr5000mg/L400mg/L18h。CSTR123PTAHRT4hCODCr400mg/L35mg/LCODCr91%。3.3-COD1000mg/LCOD>1000mg/LPTA-PTA、、、21。-UASB+、AF+、IC+、+A/O-1。1-Table1ComparisonoftheeffectbetweenanaerobicprocessandaerobicprocessCOD/mg·L-1COD/mg·L-1COD/mg·L-1COD+A/O24451~481375~40783.1~96.313%80%+2268000~14000200011080%~85%90%+23550022006060%~70%97%UASB+MBR22400080020~5080%94%A1/O1+A2/O2271110A1/O1195A1/O18682%92%A/O+MBR25291~713—3094%22UASB++MBR+UF+ROPTA、UASBCOD4000mg/LUASB800mg/LMRR+MBR20mg/LMBR。23-COD<60mg/L。24+A/OA/OA/OA/OA/O。25A/O+MBRPTASRT。+A/O+CarrouselPTA。4PTA4.1、<100mg/L、<200mg/L28。、、。、。4.2NPMgFe。。UBF+2PTACOD∶N∶P1000∶5∶11000∶12.5∶2.529。4.3pHpH。30PTA25~45℃pH5.5~8.5COD80.5%~89.6%36.8℃pH7.2CODpH。Li31PTA33374352℃COD77.4%91.9%87.4%66.1%TA77.6%94.0%89.1%60.8%。37℃CODTA。5。。CH4CO2。BABACH4CO2。。PTA222017。、、、++A/O、+2、2A/O。PTA、NPMgFepHPTA。PTACOD1000mg/L。PTA、PTA。1.PTAJ.201440743-47.2VERMASPRASADBMISHRAIM.AdsorptionKi-neticsandThermodynamicsofCODRemovalofAcidPre-treatedPetrochemicalWastewaterbyUsingGranularActi-vatedCarbonJ.SeparationScienceandTechnology20144971067-1075.3WANGCLIUCPEILetal.ExperimentalandModel-ingStudyofPureTerephthalicAcidPTAWastewaterTransportintheVadoseZoneJ.EnvironmentalScienceProcesses&Impacts2015172389-397.4.J.2013352103-106.5.PTAJ.201399-1026LIUCMWANGZY.StudyontheProcessofPTAWastewaterTreatmentJ.AdvancedMaterialsResearch2014955-9592415-2418.7.J.20021959-11.8.J.201540395-98.9ENGELHARDTGWALLNFERPRRASTHGetal.Metabolismofo-PhthalicAcidbyDifferentGram-neg-ativeandGram-positiveSoilBacteriaJ.ArchivesofMi-crobiology19761091/2109-114.10.J.19951341-5.11.M.1990.158-163.12RIBBONSDWEVANSWC.OxidativeMetabolismofPhthalicAcidbySoilPseudomonadsJ.JournalofBio-chemistry1960762310-318.13.J.1990104464-470.14.J.2013250-51.15CHENGSSHOCYWUJH.PilotStudyofUASBProcessTreatingPTAManufacturingWastewaterJ.WaterScienceandTechnology1997366/773-82.16FAJARDOCGUYOTJPMACARIEHetal.Inhibi-tionofAnaerobicDigestionbyTerephthalicAcidandItsAromaticByproductsJ.WaterScienceandTechnology199736683-90.17KIMJYWOOSHLEEMWetal.SequentialTreat-mentofPTAWastewaterinaTwo-stageUASBProcessFocusingonp-ToluateDegradationandMicrobialDistri-butionJ.WaterResearch20124682805-2814.18.PTAJ.2011373116-119.19.PTAJ.2003147-48.20.MBR+CSTRJ.2006274278-280.21.J.201439129-34.22.UASB++MBR+UF+ROPTAJ.2011365118-122.23.PTAJ.2012288103-105.24.+A/OJ.200935369-72.25.A/O-MBRPTAJ.2011311064-67.26./PTAJ.2015421-24.27.A/OPTAJ.199415647-50.28.Co-MnPTAJ.200873232-234.29.PTACODJ.201339855-58.30.PTAD.2004.31LIXMAKMENGLetal.PerformanceandMicrobialCommunityProfilesinanAnaerobicReactorTreatingwithSimulatedPTAWastewaterFromMesophilictoTher-mophilicTemperatureJ.WaterResearch20146157-66.323PTAReviewofBiologicalTreatmentProcessofPTAWastewaterQIAOXuDUYiGUOLeiJiangsuFangyangWaterAffairsCo.Ltd.Lianyungang222000ChinaAbstractPurifiedTerephthalicAcidPTAwastewatercontainsalargenumberofaromatichydrocarbonorganiccompoundsincludingrefractoryorganiccompoundsofTAandmethylbenzoicacid.InthisarticlethemechanismsofaerobicdegradationandanaerobicdegradationofaromatichydrocarbonsaswellasTAdegradationinPTAwastewaterareanalyzed.Therateofaerobicdegradationissignificantlyhigherthanthatofanaerobicdegradation.AtpresentresearchonPTAwastewatertreatmentisfocusedonaerobictreatmentandanaerobictreatmentproces-ses.Sometechnologiesofaerobicanaerobicandaerobic-anaerobictreatmentsaswellastheireffectsareintro-duced.Aerobic-anaerobictreatmentissummarizedtobetheoptimaltreatmentprocessincomprehensiveconsidera-tionofinvestmentenergyconsumptionsludgevolumeoperationandprocessingefficiency.Vortexflowanaerobicreactorplustwo-stageaerobictreatmenthydrolysisplusA/Oandtwo-stageA/Oarecommoncombinations.Fur-thermoretheinfluencesofCoMnnutrientstemperatureandpHonthebiologicaltreatmentofPTAwastewaterarediscussed.InadditionthedevelopmentprospectofresearchtrendsinPTAwastewatertreatmenttechnologyisalsopresented.KeywordsPTAwastewateraerobicdegradationanaerobicdegradationbiologicaltreatmentTAdegradation櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊櫊19theadsorptionprocessofmineralclayandir
本文标题:PTA废水生物处理工艺综述
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