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A/O1,2,1,1,1,1,1,1(1./,541004;2.,100590):A/O,,、,Box-BehnkenA/O,。:400mg/L,,45.1%76.3%;200mg/L,20%50%。3.5mg/L,55.9%89.4%;1.0mg/L,25.0%59.5%;,,,2.0mg/L。Box-Behnken,;R2=0.9769,P=0.001,,;:3.1mg/L,0.35cm3/s,55.6cm,,49.93%。:A/O;;;:X703.3:A:1004-874X(2011)11-0158-04StudyonnitrogenremovalandprocessoptimizationwithA/OintegratedbiologicalaeratedfilterSUCheng-yuan1,2,LVHong-hong1,LIFu-ying1,WANGJia1,LIYu-qiang1,CAOXiao-jie1,ZHUJiang-nan1(1.SchoolofEnvironmentandResources,GuangxiNormalUniversity/TheGuangxiKeyLabofEnvironmentalEngineeringProtectionandAssessment,Guilin541004,China;2.SchoolofMunicipleandEnvironmentalEngineering,HarbinInstituteofTechnology,Harbin150090,China)Abstract:ThispaperinvestigatedtheremovalnitrogenwithA/OintegratedbiologicalaeratedfilteratdifferentorganicconcentrationofinflowandDOinaerobicsegment.Thethree-factorandthree-levelBox-Behnkenwasutilizedformodelingandoptimizationconditions.Inthiscase,removalTNwasselectedasoneresponsevalue,whiletheDO,filterheightandfiltrationratewereconsideredaseffectfactors.Theresultsshowedthatwhentheorganicconcentrationofinflowwas400mg/L,thenitrogenremovalwaswell.TheremovalrateofTNandammoniawere45.1%and76.3%.However,whentheorganicconcentrationwas200mg/L,theywere20%and50%.WhentheDOinaerobicsegmentwas3.5mg/L,theremovalrateofTNandammoniawere55.9%and89.4%.ButtheDOwasdescendedin1.0mg/L,theremovalrateofTNandammoniawereonly25.0%and59.5%.TheDOwashigher,thenitrogenremovalwaswell.Buttheenergyconsumptionwasgreater.SothatitcouldcontroltheDOat2.0mg/L.Theinteractionoffilterheightandfiltrationratewassignificantfactor.Thedeterminatecoefficientofmodelwas0.9769andtheprobabilitypvaluewas0.001.Itcouldprovideawellexplanationoftherelationshipsbetweentheindependentvariableandtheresponse.TheoptimumconditionsweretheDOwas3.1mg/L,filterheightwas55.6cmandfiltrationratewas0.35cm3/s.Undersuchconditions,theremovalTNwas49.93%.Keywords:A/Ointegratedbiologicalaeratedfilter;nitrogenremoval;dissolvedoxygen;responsesurfacemethodology、,、,、、、,[1-3]。A/O,DesignExpert7.0,Box-BehnkenA/O,,。11.1A/O,2m,10cm,30cm,,,,,1∶2(1)。,16℃,CODCr230~290mg/L,35~40mg/L,23~30mg/L。,3~5mm,55%~78%,。1.2,CODCr,NH+4-N:2011-04-20:;:(1981-),,,,E-mail:suchengyuan2008@126.com201111158DOI:10.16768/j.issn.1004-874x.2011.11.0119080706050403020100(%)123456789103CODcr=200mg/LCODcr=300mg/LCODcr=400mg/L6050403020100(%)123456789104DO=1mg/LDO=2mg/LDO=3.5mg/L5045403530252015105012345678910(%)2CODcr=200mg/LCODcr=300mg/LCODcr=400mg/L,TN。22.12.1.12mg/L,200、300、400mg/L,A/O2。2,200、300mg/L,20%30%,15.3%。400mg/L,,45.1%,,A/O。,C/N,。,,,。C/N,。,,A/O,[4]。2.1.22mg/L,200、300、400mg/L,A/O3。3,。200、300mg/L,44%56%;400mg/L,76.3%,C/N,。2.22.2.1300mg/L,1.0、2.0、3.5mg/L,A/O4。4,1.0mg/L,25.0%;2.0mg/L,32.6%;3.5mg/L,55.9%。,。,,,2mg/L。2.2.2300mg/L,1.0、2.0、3.5mg/L,A/O5。5,1.0mg/L,;2.0、3.5mg/L,。3.5mg/L,11592Box-Behnken123456789101112131415X1101-1010-1100-10-10X20-11000-10-101-1110X31-1010-11-100-10100Y(%)39.621.135.134.248.130.624.318.430.847.730.521.140.836.448.91Box-Behnken(mg/L)(cm)(cm3/s)x1x2x3X1X2X3-12300.1503500.3014700.451009080706050403020100(%)123456789105DO=1mg/LDO=2mg/LDO=3.5mg/L80%。,,,,,A/O。,,,[1,4],2mg/L。2.3A/O2.3.1,、,Box-BehnkenA/O,1。2.3.22。DesignExpert7.0,2,:Y=48.233+3.25X1+5.687X2+4.788X3-7.929X1X1-2.75X1X2-1.7X1X3-9.454X2X2+1.775X2X3-9.6041X3X32.3.36~8。6~8,,。,[5-6],。Y,:3.1mg/L,0.35cm3/s,55.6cm,,49.93%。5042.2534.526.75191.000.500.00-0.50-1.00-0.500.000.501.00(cm)(mg/L)-1.001.000.500.00-0.50-1.00-1.00-0.500.000.501.0044.255539.236924.181129.199734.218334.2183(mg/L)(cm)6R13(1)400mg/L,,45.1%76.3%;200mg/L,20%50%,C/N,,。(2)1.0mg/L,160R150423426181.000.500.00-0.50-1.00-0.500.000.501.00(cm3/s)(mg/L)-1.001.000.500.00-0.50-1.00(cm3/s)-1.00-0.500.000.501.00(mg/L)39.70644.391939.70635.020130.334325.6484725.0%;3.5mg/L,55.9%,80%。,,,2mg/L。(3)Box-Behnken,,。R2=0.9769,p=0.001,,;:3.1mg/L,0.35cm3/s,55.6cm,,49.93%。:[1].UBAF[D].:,2008.[2],,.A/O[J].,2006,22(23):84-87.[3],,.[J].,2005,27(3):72-75.[4],,.A2/O[J].,2007,33(15):8-10.[5],,.[J].,2011,32(2):98-103.[6],,.Box-Behnken[J].,2010,32(3):389-392.5042.2534.526.75191.00R10.500.00-0.50-1.00-0.500.000.50(cm3/s)(cm)1.00-1.001.000.500.00-0.50-1.00(cm3/s)-1.00-0.500.000.501.00(cm)30.25844.932640.04135.149530.25825.366530.2588161
本文标题:AO一体化曝气生物滤池脱氮效能及其运行优化研究宿程远
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