您好,欢迎访问三七文档
当前位置:首页 > 商业/管理/HR > 管理学资料 > SBR中不同曝气方式下CANON工艺的启动与运行李冬
49920179JOURNALOFHARBININSTITUTEOFTECHNOLOGYVol.49No.9Sep.2017DOI10.11918/j.issn.0367-6234.201604003SBRCANON11111121.1001242.150090CANONCANONDO.CANON.CANONSBRSBRR1SBRR2CANON.R1R221、27CANON.HRTR1R225d、33dCANON.R1R284.32%、73.62%.SBR//R124.7%、58.54%86.R1AOBAnAOBNOB..X703.1A0367-6234201709-0109-08Start-upandlongtermoperationofCANONinsequencingbatchreactorwithdifferentaerationpatternsLIDong1LIXiaoying1YANGJie1LYufeng1LIANGYuhai1WANGYanju1ZHANGJie121.KeyLaboratoryofBeijingforWaterQualityScienceandWaterEnvironmentRecoveryEngineeringBeijingUniversityofTechnologyBeijing100124China2.StateKeyLaboratoryofUrbanWaterResourceandEnvironmentHarbinInstituteofTechnologyHarbin150090ChinaAbstractIntheoperationofcompletelyautotrophicnitrogenremovalovernitriteCANONprocessarecentlydevelopednewtypeofnitrogenremovaltheimpropercontrolofDOcaneasilyleadtothedeclineorevencollapseofthenitrogenremovalrate.ThekeytothestableoperationoftheCANONprocessisreasonablecontrolofdissolvedoxygeninsidethereactor.GivencontroversiesofthepresentfindingsonthestartupandlongrunningofCANONindifferentaerationmodesthestartupandperformanceofCANONprocessweretestedinSBRwithtwodifferentaerationstrategies—intermittentaerationR1andthecontinuousaerationR2.ResultsshowedthattheCANONwassuccessfullydevelopedinbothR1andR2within21dand27d.AfterextendedaerationdamageCANONofR1andR2fullyrecoveredwithin25dand33donconditionsofHRTchangeandruncycleincrease.ThefinalTNremovalratesofR1andR2were84.32%and73.62%.Theresultsfurthershowedthatbothalternatingnitritation/anammoxandsimultaneousnitritation/anammoxcontributedtoN-removalinSBRandtheircontributionsinR1accountedfor58.54%and24.7%86d.ThebioactivityofammoniaoxidizingbacteriaAOBandanaerobicammoniaoxidizingbacteriaAnAOBinR1washigherthanthatofR2whilethebioactivityofnitriteoxidizingbacteriaNOBshowedacontraryresult.IntermittentaerationisaneffectivemeanstoobtainstablyhighTNremoval.KeywordsCANONintermittentaerationcontinuousaerationextendedaerationSBR2016-04-022014000026833TD021976—1938—lidong2006@bjut.edu.cnCANON、、1.CANON2-3.CANONDO.CANON.CANON.Ma4SBR5SBBRYang6MBBRCANONSobotka7SBRCANONCorbalá-Robles8SBRCANON.CANON.2SBRCANONCANONCANONCANON.11.11.SBRR1、R235cm13cm4L66.7%.5cm.、、.、.!#$%&’()1—2—3—4—5—6—、、、7—8—pH9—DO1Fig.1Schematicdiagramofexperimentaldevice1.21500mg/LR1R2NH42SO4NaHCO3NH4+-NI、II9IEDTA5000mg/LFeSO45000mg/L.IIEDTA15000mg/L、ZnSO4·7H2O430mg/L、CoCl2·6H2O240mg/L、MnCl2·4H2O990mg/L、CuSO4·5H2O250mg/L、Na2MoO4·2H2O220mg/L、NiCl2·6H2O190mg/L、Na2SeO4·10H2O210mg/LH3BO414mg/L.1.1Tab.1WaterqualityduringthetestperiodρNH4+-N/mg·L-1CaCO3/mg·L-1MgSO4·5H2O/mg·L-1CaCl2/mg·L-1KH2PO4/mg·L-1Ⅰ/mL·L-1Ⅱ/mL·L-160~801600~1800804040111.3SBR15min、、40min、3min.20~25℃67.7%.1/30min/30minDO0.38mg/L.2DO0.23mg/L.2CANON、.1.4DO、T、pHWTWMLSS.NH4+-NNO2--NN-1-NO3--N10.85~90R1R21L2.CANON、Anammox·011·49AOBAnAOB、AnAOBNOB.325℃pH7.6.CANON80mg/L0.25L/min1h、、.Anammox45.5mg/L34.5mg/L1h、、.80mg/L0.25L/min1h、.CANONAnammox12vCANONAnammox=ρTN-ρTNt·ρMLSS1v=ρNO-3-N-ρNO-3-Nt·ρMLSS.222.1CANONCANONΔρTNΔρNO3--N811ΔρTN/ΔρNO3--N8ΔρTN/ΔρNO3--N8NOBΔρTN/ΔρNO3--NNOB12.2R1R22dAOB.7dR1R24.2NOB.8~21dR1ΔρTN/ΔρNO3--NR2.21R1ΔρTN/ΔρNO3--N7.88CANON2a.R227ΔρTN/ΔρNO3--N7.6CANON.2.11R148.92%、39.9%R246.58%、37.71%R1R2.21R182.79%、70.75%R274.73%、62.57%.R1R2.!#$%&’!$’!&’#’%(!!(&&()!*+!#$%&’(*),-./,-.+01!*+#$,*2!#$%&!#$,*2!#$%&+#$,*2!#$%&!#$,*2’!$’!&’#’%!#$%&’(*),-./,-.+01!*#3$(%)-./#3$(%)-./(!!(&&())(!*++#$,!#$,!#$%&’(-./aR1bR22R1、R2CANONFig.2Start-updiagramofCANONprocessinR1R2·111·9SBRCANON2.2CANON90%SBR13.AnAOBNOB.AnAOBAOBNOBAnAOB.Lackner14CANON.、、1h1h1h30min30minCANONCANON.CANON10dR1R210d..3R130~40dR237~47dR1R280%.AOBAnAOBNOBAOBAnAOB.ΔρTN/ΔρNO3--NR17.695.23R27.65.2NOBAnAOB.1522±1℃NOBNOB..!#$%&’!$’!&’#’%!()!#$%&’(()*+,-*+,)./!*+#$,(0!#$%&!#$,(0!#$%&+#$,(0!#$%&!#$,(0’!$’!&’#’%!#$%&’(()*+,-*+,)./!*#1$2%3-./#1$2%3-./%%2222$$2112##24!()+#$,!#$,!#$%&’(-./332%%2222$$2112##24aR1bR23CANONFig.3PerformanceofthereactorinrunningCANONprocessunderdifferentaerationpatternsafterextendedaerationR1R24047.Abeling16FA1.0~10mg/LNOBAOBRALNOB17HRT5hRAL0.8kg/m3·dFANH31.14~4.5mg/LDOCANON.30~7dΔρTN/ΔρNO3--N·211·495.2NOBNOB..R1R2.R165CANON.R281.R1R225、33dR1NOB18AOBNOB“”AOBNOB19AnAOB20.Kornaros21NOBNOB.R1R2R190R10.157kg/kg·d84.36%R20.14kg/kg·d73.62%.CANON.HRTFACANON.2.32.3.14abR1、R2CANON86DO.4aDO0.38mg/LTNAOBANAMMOXTNTN.8.0mg/LAnAOB1.23mg/LTN17.83mg/L..TN1.37、12.92mg/L.4bR2DO0.23mg/LR2120min2.53mg/L120min.12.56、22.92mg/L.R1R2.!#$%&’(&&’)&&*+,+-+.+/+$+)+(+0+++1/+1$+1)+1(+10++)+.+*+0(+0/+0,+(0+($+(-+)++!23456’27389:&0;7!;2#389:&0$*+,+-+.+/+$+)+(+0+++1/+1$+1)+1(+106’27389:&0;7!;2#389:&0$)+.+*+0(+0/+0,+(0+($+(-+)++!2345+aR1bR24DOFig.4ChangeofnitrogenandDOduringatypicalcycle·311·9SBRCANON.2.R130.30mg/L53.95mg/LAnAOBCANON.R1NOBAnAOB22.53.95~30.30mg/LCANON2.72mg/LΔρNO3--N/ΔρNH4+-N0.115CANON1∶0.11AOBAnAOBNOB.30.30mg/L24.25mg/L.6.02mg/LΔρNO3--N/ΔρNH4+-N0.2480.26..R1/SNA/ANA5.R2/.66.67mg/L7.85mg/LΔρNO3--N/ΔρNH4+-N0.1180.11.2/Tab.2Changeofnitrogeninaerobic/anaerobicduringatypicalcycle/mg·L-1/mg·L-1/mg·L-1ΔρNO3--N/ΔρNH4+-NR153.9524.2530.302.726.020.1150
本文标题:SBR中不同曝气方式下CANON工艺的启动与运行李冬
链接地址:https://www.777doc.com/doc-6541123 .html