改良UCT分段进水工艺处理生活污水性能优化研究葛士建

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32720117ENVIRONMENTALSCIENCEVol.32No.7Jul.2011UCT11*11121.1001242.100038UCTCOD/NCOD/N、COD/PTN/P..COD0.79~0.93kg/m3·d4COD43.7±8.35mg/L83.8±3.86%COD60.2%~76.2%.40%∶30%∶30%88.2%32.8%NH+4-NTN0.21±0.20mg/L7.90±1.27mg/L.32.6%~39.5%97.2%.COD/N4.64~7.41R2=0.96COD/PTN/P35.0~92.56.24~12.5R2=0.87R2=0.89.SVI82.6±4.99mL/g.UCTX703.1A0250-3301201107-2006-072010-08-292010-10-272008ZX07317-007-105PHR20090502ykj-2010-37381987~E-mailgl-222@tom.com*E-mailpyz@bjut.edu.cnOptimizationofaModifiedUCTStepFeedProcessTreatingMunicipalWastewaterGEShi-jian1PENGYong-zhen1CAOXu1WANGShu-ying1YANGAn-ming121.KeyLaboratoryofBeijingforWaterQualityScienceandWaterEnvironmentRecoveryEngineeringBeijingUniversityofTechnologyBeijing100124China2.BeijingDrainageGroupCo.Ltd.Beijing100038ChinaAbstractApilot-scalemodifiedUCTstepfeedprocesswasproposedtotreatthemunicipalwastewaterwithlowerCOD/Ninalarge-scalewastewatertreatmentplant.EffectsofinfluentdistributionratiosandnutrientsratiosCOD/N、COD/PandTN/Ponnutrientsremovalcapabilitieswereimportantlyinvestigated.Theremovalmechanismsoforganicsandnutrientsandsludgecharacteristicswereultimatelydiscussed.Accordingtothecontinuousexperimentsthestableandhighprocessperformancewasobtained.TheaverageCODremovalefficienciesandeffluentconcentrationof83.8±3.86%and43.7±8.35mg/LwereachievedintheinfluentCODloadingof0.79-0.93kg/m3·d.TheCODremovalinanaerobicandanoxiczonesaccountedfor60.2%-76.2%.Withtheinfluentdistributionratioof40%∶30%∶30%asmuchas88.2%ofTNremovalefficiencywasobserved.Itshouldbeconsideredtheremovalof32.8%throughsimultaneousnitrificationanddenitrificationprocess.TheaverageeffluentNH+4-NandTNwere0.21±0.20mg/Land7.90±1.27mg/Lrespectively.Itwasextremelyimportantthatasmuchas32.6%-39.5%ofthedenitrifyingphosphorusaccumulationorganismscontributedtothehighphosphorusremovalefficiencyof97.2%.AlinearpositiverelationshipwasobservedbetweennitrogenremovalefficiencyandCOD/Nintherangeof4.64and7.41R2=0.96.PhosphorusremovalefficiencywasfoundtobeafunctionoftheinfluentCOD/PandTN/Pvaryingfrom35.0to92.5andfrom6.24to12.5respectivelyR2=0.87andR2=0.89.InadditionthegreatsludgesettleabilitywasobtainedwiththemeanSVIof82.6±4.99mL/g.KeywordsstepfeedinflowdistributionratiosnitrogenandphosphorusremovalsimultaneousnitrificationanddenitrificationSNDdenitrifyingphosphorusremovalUniversityofCapeTownUCT.-.A/O、//A/A/OUCT12.COD/N.COD/N.DOI:10.13227/j.hjkx.2011.07.0327UCT3①②③.23.A/OA/O、4~8..9.UCTCOD/N.UCT.11.1UCT1、.340L50cm×60cm×125cm13、..50cm60°90cm88L、.、、.、.1.2.3.4.5.6.7.8.AN.DN.1UCTFig.1Schematicdiagramofpilot-scalemodifiedUCTstepfeedBNRprocess420%∶30%∶50%、30%∶40%∶30%、40%∶30%∶30%、50%∶30%∶20%43.、COD/NCOD/P4.63~7.4135.0~92.5..1.2A/A/O.COD308±172mg/LTN52.9±17.1mg/LNH+4-N51.0±18.8mg/LNO-2-N0.07±0.32mg/LNO-3-N0.91±1.39mg/LPO3-4-P3.92±5.49mg/LTP6.43±6.22mg/L.15d.1.30.45μmNH+4-N、NO-2-N、NO-3-N、PO3-4-P、COD10WTWlevel-2pHpHWTWpH/oxi340i700232ORPDOMLSSMLVSS.1.4SNDSNDSND1~4.NSND=Ninfluent-Ndenitrification-Nassimilation-Neffluent1Ndenitrification=NDN1+NDN2+NDN32Nassimilation=MLSSwaste×fVSS/SS×Vwaste×fN/biomass3SNDefficiency=NSNDNinfluent×100%4NSND、NdenitrificationNassimilationSND、g/dNinfluentNeffluentg/dNDN1、NDN2NDN3g/dMLSSwasteg/Lfvss/ssMLVSSMLSSVwasteLfN/biomass12.39%11.22.1UCT.24COD.183.6~402.8mg/L43.7±8.35mg/L83.8±3.86%.COD.14COD76.2%、70.4%60.2%COD、COD/N..24CODFig.2VariationprofilesofCODwithfourinfluentdistributionratios2.2.313.HRT12.30d50%HRT.230%0.09mg/L12.7mg/L.40%84.9%.450%.1314.Larrea7A/O40%∶40%∶20%~33%∶33%∶34%Vaiopoulou1460%∶25%∶15%.340%∶30%∶30%80027UCT34Fig.3Variationprofilesofnitrogenwithfourinfluentdistributionratios.、.A/O、A2/O.11ΔN.1~442.SND41.5、8.65、18.68.74g/d.40%∶30%∶30%SND32.8%88.2%.SND2①1Table1Effectofinflowdistributionratiosonthemodifiedstepfeedprocessperformance/%/mg·L-112311ΔPΔN22ΔN32ΔN20∶30∶5030∶40∶3040∶30∶3050∶30∶20COD269.786.561.538.259.940.862.949.048.9NH+4-N56.714.77.890.2119.00.7220.48.438.31NO-3-N0.221.054.038.034.393.7811.610.57.4313.16.3812.9NO-2-N0.020.020.330.030.000.000.080.0040.01PO3-4-P12.411.80.603.664.812.933.212.442.47COD289.5105.347.840.365.439.453.249.447.8NH+4-N49.919.312.80.4121.30.7513.60.000.00NO-3-N0.010.873.999.682.952.6411.311.912.4410.55.5910.2NO-2-N0.000.010.440.050.030.010.060.010.00PO3-4-P6.3621.0514.07.051.271.840.951.021.081.11COD289.0128.849.744.360.441.951.140.132.7NH+4-N55.626.819.50.6118.60.9213.10.000.00NO-3-N0.180.131.296.015.641.378.5810.741.566.688.166.53NO-2-N0.030.030.530.080.270.000.270.090.08PO3-4-P5.9829.79.3620.30.330.520.380.520.410.42COD287.6156.765.743.362.848.348.947.947.2NH+4-N54.3930.922.64.5223.32.039.430.010.00NO-3-N0.140.996.7517.67.819.3215.815.89.5516.02.9615.7NO-2-N0.310.020.610.031.260.250.390.400.35PO3-4-P5.5831.211.220.00.210.510.040.310.080.099002322UCTTable2NitrogenbalanceanalysesofthemodifiedUCTstepfeedprocess/%20∶30∶5030∶40∶3040∶30∶3050∶30∶20Ninfluent/g·d-157.850.856.756.0Nwaste/g·d-114.09.4912.711.7Ndenitrification/g·d-118.844.833.434.9Neffluent/g·d-121.610.46.7416.4NSND/g·d-111.58.6518.68.74SND/%20.017.032.815.6TN/%62.779.688.271.0MLVSS5500、47504100mg/LDO1.5~2.0mg/L0.05~0.8mg/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