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OCO525011。OCO20h、10、4、6hOCODO3.0~4.0mg/LCOD、100、15、30mg/L90%、70%50%。OCO。OCOCODSlaughteringwastewatertreatmentbyOCOprocessAbstractUsuallyslaughteringwastewaterisrichinorganicsandnitrogenandsometimesnitro-gencontentishigherthandischargestandard.OCOprocesswasadoptedtotreatslaughteringwastewaterinordertoreducenitrogencontent.InthebiologicalexperimentofcarbonremovalanddenitrificationwhentotalhydraulicresidenttimeHRTwas20htheHRTofanaerobiczoneanoxiczoneandaerobiczoneinOCOreactorwere10h4hand6hrespectivelyandwhendissolvedoxygenDOconcentrationinaerobiczonewas3mg/L~4mg/LtheremovalratesofCODammonianitrogenandtotalnitrogenwererespectivelyover90%70%and50%andeachconcentrationintreatedwaterwere100mg/L15mg/Land30mg/Lwhichhadreachedthenationaldischargestandard.ItwasprovedinexperimentalstudythatOCOprocesswasefficientinbiologicalremovalofcarbonandnitrogenwhichcouldbeanewtechnologyforslaughteringwastewatertreatment.KeywordsslaughteringwastewaterOCOprocessbiologicaldenitrificationCOD1~4。檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪檪6GUERARDF.GUIMASL.BINETA..Productionoftu-nawastehydrolysatesbyacommercialneutralproteaseprep-arationJ.JournalofMolecularCatalysisBEnzymatic200219~202489~4987.J.2007323100~1038.M.19933~49.D.2007.10.J.2007771078~109711.M.20046~812.J.200728548~5213.J.200122392~9414SENR.SWAMINATHANT..Applicationofresponse-sur-facemethodologytoevaluatetheoptimumenvironmentalcondi-tionsfortheenhancedproductionofsurfactinJ.AppliedMi-crobiologyandBiotechnology1997474358~3632011-01-04080103010782008GA710021。1986-。1976-。23MEATINDUSTRY20113359。COD、BOD5。“”。A/O、A/A/O、。OCO56。OCO。11.1OCOOCOOCO1。1OCOOCO。OCO。OCO5∶∶=1∶2.3∶3。350%C/N6。、OCO∶∶=5∶2∶3。OCO800mm560mm700mm0.25m3。、。1.2SS80%COD、BOD530%~50%。COD≤1000mg/LBOD5≤480mg/LSS≤150mg/LNH3-N≤60mg/LBOD5/CODB/C0.43~0.58。1.3OCO。。。24h12h30min。5~6d。22.1OCOOCOpH、DO、3320113359MEATINDUSTRYMLSS、HRT、、BOD5/NO-x—NC/N。OCO。2.1.1135℃5℃28℃20℃7。20~40℃15℃。2pHH+pHpHpH8.0~8.4pH6.57。pH1g7.1gpH6.5~7.5。3DODO8。DO2.0mg/LCODDO。DODO0.5mg/L。DO3.0~4.0mg/LOCO。2.1.21MLSSMLSS3000~5000mg/LOCO。3000mg/L5000mg/L。2HRTHRT10hHRT4hHRT6h5∶2∶3。3。MLSS。COD0.6kg/m3·d。4C/NC/N≥4。、NO-x。C/N≥6BOD5。2.2OCOCODCO2H2O。2COD。2COD2COD100mg/L90%。OCO。2.3OCO、。N243MEATINDUSTRY20113359。34。338~60mg/LOCO15mg/L70%75%~85%。430mg/L50%。。OCO。N2。31OCO20h10h4h6h。2COD、100、15、30mg/L90%、70%、50%。3OCO。1.J.20103191~1922.J.2010336309~3123AsselinM.DroguiP.BenmoussaH.etal.EffectivenessofelectrocoagulationprocessinremovingorganiccompoundsfromslaughterhousewastewaterusingmonopolarandbipolarelectrolyticcellsJ.Chemosphere200872111727~17334DebikE.CoskunT..Useofthestaticgranularbedreactorwithanaerobicsludgetotreatpoultryslaughter-housewastewaterandkineticmodelingJ.BioresourceTechnolo-gy2009100112777~27825.OCOJ.200430817~206.J.200929479~817.J.200435361~648.J..2008372113~1152011-01-071967-。5320113359MEATINDUSTRY
本文标题:OCO工艺处理屠宰废水钟华文
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