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Eco-EnvironmentalKnowledgeWebEnvironmentalScience40320193Vol.40No.3Mar.2019SPNDPRC/N*266071C/N180min/SBRL·min·L-1.0.125L·min·L-10.025L·min·L-13h6hSPNDPR.0.025L·min·L-1、6hSPNDPRNH+4-N、NO-2-N、NO-3-NPO3-4-P0、8.62、0.060.03mg·L-1TN9.22mg·L-1TN87.08%.0.125L·min·L-10.100L·min·L-10.100L·min·L-10.075L·min·L-10.16mg·L·min-1.0.050L·min·L-10.025L·min·L-10.09mg·L·min-10.06mg·L·min-1.0.125L·min·L-10.100、0.075、0.050、0.025L·min·L-13h6hSPNDSND19.57%72.11%TN62.82%87.08%.SPNDPR、、、C/N.X703.1A0250-3301201903-1382-08DOI10.13227/j.hjkx.2018080182018-08-022018-09-195177830451708311ZR2017BEE0022017M6122091993~E-maily_yuanmengfei@126.com*E-mailelainewangxx@163.comNitrogenandPhosphorusRemovalfromLowC/NMunicipalWastewaterTreatedbyaSPNDPRSystemwithDifferentAerationandAerobicTimesYUANMeng-feiYUDe-shuangGONGXiu-zhenWANGXiao-xia*CHENGuang-huiDUShi-mingZHENJian-yuanSchoolofEnvironmentalScienceandEngineeringQingdaoUniversityQingdao266071ChinaAbstractAnanaerobic180min/aerobicoperatedsequencingbatchreactorSBRfedwithurbansewagewasoptimizedbyregulatingtheaerationquantitytoinvestigatethedeep-levelnitrogenNandphosphorusPremoval.TheamountofaerationwasregulatedbyadjustingthevolumeofgasperunitvolumeofreactorpassedinunittimewhentheunitisL·min·L-1from0.125L·min·L-1graduallyto0.025L·min·L-1andaerobictimesfrom3hto6h.TheexperimentalresultsshowthattheeffluentNH+4-NNO-2-NNO-3-NandPO3-4-PconcentrationsoftheoptimizedSPNDPRsystemwere08.620.06and0.03mg·L-1.TheeffluentTNconcentrationwasabout9.22mg·L-1andtheTNremovalefficiencywasupto87.08%.Whentheaerationquantitywasdecreasedfrom0.125L·min·L-1to0.100L·min·L-1thendecreasedto0.075L·min·L-1thenitrificationrateofthesystemrecoveredandstabilizedat0.16mg·L·min-1.Howeverwhentheaerationquantitycontinuouslydecreasedto0.050L·min·L-1andthento0.025L·min·L-1thenitrificationratedecreasedto0.09mg·L·min-1and0.06mg·L·min-1.Withreductionoftheaerationquantityfrom0.125L·min·L-1to0.1000.0750.050and0.025L·min·L-1andextensionofaerobictimefrom3hto6htheTNremovalefficiencyincreasedgraduallyfrom62.82%to87.08%andtheSNDefficiencyincreasedfrom19.57%to72.11%.ItwasproventhatreducingtheaerationquantitycanenhancetheSPNDfunctionanddeepdenitrificationbythesystemwasrealized.Byenhancingtheanaerobicintracellularcarbonstorageandaerobicphosphorusuptakedenitrifyingphosphorusremovalpartialnitrificationandendogenousnitrificationwereachieved.TheSPNDPRsystemafterreducingaerationandprolongingaerobictimewasabletorealizedeep-leveldenitrificationanddephosphorizationusinglowC/Nurbansewage.Keywordsaerationquantitysimultaneouspartialnitrification-endogenousdenitrificationphosphorusremovalSPNDPRintracellularcarbonstorageCODinsC/NratiophosphorousaccumulatingorganismsPAOsPNDOSRTNOBNO-2-N1、2.SND3~9.3SPNDPRC/NSPNDPNSNDNH+4-NAOBNO-2-NN210、、.EBPR11~14.EBPRPAOsPAOs15.DPRNO-2-NNO-3-N16.EBPRDPRPO3-4-P.17~19、DO2021、22~2526C/NSPNDPR.SPNDPRSNDSPNDPR“”27.SPNDPR28SPNDPR.C/N≤4/SBR/SRTL·min·L-1SPNDPRCOD、、SPNDPRC/N.11.1SBR13L8L./1.SPNDPR0.125L·min·L-1、3hNH+4-N、NO-2-N、NO-3-N、PO3-4-PCOD0.35、20.05、0.42、0.4763.55mg·L-1.1SPNDPR1Table1RunningparametersduringtheoptimaloperationoftheSPNDPRsystem11~28d229~53d354~77d478~97d598~118d/L888883∶83∶83∶83∶83∶8/min180180180180180/min180180300*300360SRT/d1010101010HRT/h161621.3321.3324/L·min·L-10.1000.0750.0500.0250.025DO/mg·L-1≤0.8≤0.6≤0.5≤0.3≤0.31*0.075L·min·L-10.050L·min·L-1180minNH+4-N23.15mg·L-1FA300min1.2COD176.75~572.48mg·L-1NH+4-N53.99~92.84mg·L-1NO-2-N<1mg·L-1NO-3-N<1mg·L-1PO3-4-P3~10.25mg·L-1pH7.2~7.6.SPNDPRMLSS4016mg·L-1SV21%SVI52.29mL·g-1.1.31.3.115~20μmNH+4-NNO-2-NN-1-NO-3-NPO3-4-PCOD5B-3ACODMLSSDOpHPHS-3CpH.3831401.3.2CODinsCODinsSPNDPRCODPAOsGAOs.CODinsmg·L-1=ΔCOD-1.71ΔNO-2+2.86ΔNO-3ΔCOD、ΔNO-2ΔNO-3COD、NO-2-NNO-3-Nmg·L-11.712.86NO-2-NNO-3-NCOD.1.3.3SNDSNDSPNDPRSND=1-ΔNO-2+ΔNO-3ΔNH+[]4×100%ΔNH+4、ΔNO-2ΔNO-3NH+4-N、NO-2-NNO-3-Nmg·L-1.22.1SPNDPRCOD1SPNDPRCOD、COD、CODins、CODCOD.11~28d0.125L·min·L-10.100L·min·L-1COD302.62mg·L-1COD75.25mg·L-164.83mg·L-144.64mg·L-133.08mg·L-1.CODins26.47mg·L-151.90mg·L-1.SPNDPR.COD151.31g·m3·d-1COD90.24g·m3·d-1110.36g·m3·d-1COD73.57%86.97%.1SPNDPRCODCODCODinsFig.1VariationsofCODconcentrationremovalefficiencyandCODinsduringtheoptimaloperationoftheSPNDPRsystem229~53d0.100L·min·L-10.075L·min·L-1COD293.32mg·L-1COD70.59mg·L-158.75mg·L-144.81mg·L-138.25mg·L-1.COD146.66g·m3·d-1COD103.37g·m3·d-1124.54g·m3·d-1COD77.87%84.40%.354~77d0.075L·min·L-10.050L·min·L-13h5hCOD319.24mg·L-1COD56.63mg·L-153.25mg·L-169d71.17mg·L-168.58mg·L-145.99mg·L-141.64mg·L-1.COD117.08g·m3·d-197.11g·m3·d-164d97.17g·m3·d-179.23g·m3·d-1117.35g·m3·d-1101.71g·m3·d-1COD82.94%69d78.85%86.43%.4~578~118d48313SPNDPRC/N0.050L·min·L-10.025L·min·L-15h6hCOD309.78mg·L-1COD41.47mg·L-136.18mg·L-1COD87.30%90.35%.45COD117.45g·m3·d-1102.16g·m3·d-1COD104.01g·m3·d-191.99g·m3·d-1.SPNDPRCODCOD102.16g·m3·d-1COD91.99g·m3·d-1COD90%.2~5CODins64.24mg·L-189.74mg·L-1.0.075L·min·L-10.025L·min·L-13h6hSPNDPR.2SPNDPRPO3-4-PFig.2VariationsofthePO3-4-PconcentrationandremovalefficiencyduringtheoptimaloperationoftheSPNDPRsystem2.2SPNDPR2SPNDPRPO3-4-P.11~28d0.125L·min·L-10.100L·min·L-11~1
本文标题:不同曝气量和好氧时间下SPNDP省略理低CN城市污水的脱氮除磷性能袁梦飞
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