当前位置:首页 > 商业/管理/HR > 质量控制/管理 > DPRSNED系统处理低CN城市污水与硝酸盐废水的运行特性杜世明
Eco-EnvironmentalKnowledgeWebEnvironmentalScience40220192Vol.40No.2Feb.2019DPR-SNEDC/N*266071C/NSBR//DODPR-SNED./3hDO0.5~1.0mg·L-160dSNEDPRPO3-4-P<0.5mg·L-190%COD80%SNEDCODins70%95%//45dDPR-SNEDPO3-4-P<1.1mg·L-1PO3-4-P<0.5mg·L-1、COD90%88%SNEDCODins62%90%.DPR-SNED.DPR-SNEDC/N4.DPRSNEDPAOsX703.1A0250-3301201902-0791-08DOI10.13227/j.hjkx.2018080902018-08-112018-08-265177830451708311ZR2017BEE0022017M6122091994~E-maild_shiming@163.com*E-mailelainewangxx@163.comOperatingCharacteristicsofaDPR-SNEDSystemTreatingLowC/NMunicipalWastewaterandNitrate-containingSewageDUShi-mingYUDe-shuangBIChun-xueWANGXiao-xia*CHENGuang-huiYUANMeng-feiZHENJian-yuanZHANGFanLTing-tingSchoolofEnvironmentalScienceandEngineeringQingdaoUniversityQingdao266071ChinaAbstractInordertorealizethesimultaneoustreatmentoflowC/NmunicipalwastewaterandhighnitratewastewaterasequencingbatchreactorSBRinoculatedwithactivatedsludgewasusedtoinitiatethedenitrifyingphosphorusremovalcoupledwithsimultaneousnitrificationandendogenousdenitrificationDPR-SNED.Theanaerobic/anoxic/hypoxicdurationsanddissolvedoxygenDOconcentrationwereappropriatelycontrolledandthenitrogenandphosphorusremovalcharacteristicswereexamined.Theexperimentalresultsdemonstratedthatintheanaerobic/hypoxiaoperationmodewithananaerobicdurationof3handDOconcentrationof0.5-1.0mg·L-1thesimultaneousnitrificationofphosphorusremovalSNEDPRsystemsuccessfullybeganin60d.TheeffluentPO3-4-Pconcentrationwasbelow0.5mg·L-1thenutrientandCODremovalefficiencieswerestablymaintainedabove90%and80%respectivelyandtheSNEDefficiencyandCODinsefficiencyreached70%and95%respectively.Whentheoperationmodewasanaerobic/anoxic/hypoxicandnitrate-containingsewagewasaddedatthebeginningoftheanoxicstageDPR-SNEDwasachievedwiththeeffluentPO3-4-Pconcentration<0.5mg·L-1nutrientandCODremovalefficienciesabove88%and90%respectivelyandSNEDefficiencyandCODinsefficiencymaintainedat62%and90%respectively.AfterthesuccessfulinitiationofDPR-SNEDenhancedintracellularcarbonsstoragewasachievedbyphosphorus-andglycogen-accumulatingorganismsusingthelimitedcarbonsinrawmunicipalwastewatertoprovidesufficientcarbonsourcesforsubsequentnutrientremoval.InadditiontheendogenouspartialdenitrificationensuredtheefficientnitrogenremovalperformanceoftheDPR-SNEDsystematlowC/Nconditionsaverage4.KeywordsdenitrifyingphosphorusremovalDPRsimultaneousnitrificationendogenousdenitrificationSNEDphosphorousaccumulatingorganismsPAOsmunicipalwastewaternitrate-containedsewage、1..、、、、2.40-3.1molNH+4-N1.32molNO-2-N0.26molNO-3-N.TN42..DPR5~8.PHA“”910.SNEDPHA11.DPR-SNEDC/N.、.SNEDNO-x-NNO-2-N+NO-3-NNO-x-N12.C/N.SBRDPRSNEDDPR13~16SND17181920A2/O+MBBRA2/O-BCOC/N、TNPO3-4-P88%、80%96%21SBRSNEDEBPRDOSNEDTN75%84%.DPRSNEDC/N.C/N///DPR-SNED./DO0.5~1.0mg·L-1SNEDPR//SNEDPRDPR-SNED.C/N.11.1SBR113L8~11L.SBR/1~60d8L4C/N3L100mL1.1.2.3.4.pH5.Ph68.79.10.11.12.13.14.15~17.18.1SBRFig.1ExperimentaldevicediagramoftheSBRSBR//61~105d11L2C/N3L3L100mL1.2500±300mg·L-1.1.2SBRMLSS3000mg·L-1SV%30%.SBRC/N2972DPR-SNEDC/N2.pH7.2~7.6C/N4.SBRNH+4-N、NO-2-NPO3-4-P1mg·L-1COD10mg·L-1NO-3-N28.09~31.2mg·L-1.1Table1Statisticsofoperationparametersineachphase11~18d219~37d338~60d461~105d/L88811//////min180180180180/min———180/min1501501501503∶83∶83∶86∶11HRT/h14.6714.6714.6718.08DO/mg·L-10.5~1.00.5~1.00.5~1.00.5~1.02Table2Statisticsofqualityeffluentwastewaterineachphase11~18d219~37d338~60d461~105dNH+4-N/mg·L-136.09~66.7036.45~73.7636.78~81.5227.18~73.18NO-2-N/mg·L-1<1<1<1<1NO-3-N/mg·L-1<1<1<1<1PO3-4-P/mg·L-12.07~6.902.91~8.192.07~8.771.66~9.62COD/mg·L-1161.20~287.02210.30~333.20184.70~312.67228.26~355.901.315~20μmNH+4-NN-1-NO-2-NNO-3-NPO3-4-P225B-3ACODCODMLSS23SV100mL30minSVISVMLSS24DOpHPHS-3CpH.1.4CODinsCODinsDPR-SNEDCOD1CODins=ΔCOD-2.86ΔNO-3+1.71ΔNO-21ΔCOD、ΔNO-2ΔNO-3COD、NO-2-NNO-3-Nmg·L-11.712.86NO-2-NNO-3-NCOD.1.5CODinsCODinsDPR-SNEDCOD221CODins=1-2.86ΔNO-3+1.71ΔNO-2Δ()COD×100%2ΔCOD、ΔNO-2ΔNO-3COD、NO-2-NNO-3-Nmg·L-11.712.86NO-2-NNO-3-NCOD.1.6SNEDSNEDDPR-SNED123SNED=1-ΔNO-3+ΔNO-2ΔNH+()4×100%3ΔNH+4、ΔNO-2ΔNO-3NH+4-N、NO-2-NNO-3-Nmg·L-1.22.1DPR-SNED4DPR-SNEDPO3-4-P2.211~18dPO3-4-P4.04mg·L-1PO3-4-P2.78mg·L-1397402DPR-SNEDPO3-4-PFig.2VariationinthePO3-4-PconcentrationduringtheoperationalperiodoftheDPR-SNEDsystem5.91mg·L-17.17mg·L-1PO3-4-P60.86%.3DPR-SNEDNH+4-NFig.3VariationintheNH+4-NconcentrationduringtheoperationalperiodoftheDPR-SNEDsystem219~37d12.02mg·L-130.77mg·L-122.16mg·L-11PO3-4-P3.85mg·L-1PO3-4-P79.6%.338~60dPO3-4-P.PO3-4-P4.68mg·L-1PO3-4-P0.06mg·L-118.09mg·L-122.71mg·L-1.PO3-4-P98.24%.461~105d.PO3-4-P5.1mg·L-1.PO3-4-P63d6.68mg·L-169d1.65mg·L-170d0.57mg·L-1.PO3-4-P0.5mg·L-1.C/N.2.2DPR-SNED3DPR-SNEDNH+4-N.11~18d1~5dNH+4-N9.5mg·L-122.95mg·L-16~4972DPR-SNEDC/N10d5.02mg·L-1.1~10dNH+4-N73.73%.11~18dNH+4-NNH+4-N90%.219~37dNH+4-N2.43mg·L-1NH+4-N94.76%100%.338~60d.NH+4-N95%NH+4-N0.23mg·L-1.NO-2-NNO-3-N10.4mg·L-13.74mg·L-11.19mg·L-14.39mg·L-12.4.NO-2-NNO-3-NSNED.NH+4-N.461~105d//.NH+4-N0.02mg·L-1NH+4-N100%.1~3/4//.2.3DPR-SNEDCOD4DPR-SNEDCOD.11~18dCOD219.33mg·L-1COD73.81mg·L-160.63mg·L-1COD.CODinsCODins41.52mg·L-189.22%COD67.77%COD5.91mg·L-12.1.
本文标题:DPRSNED系统处理低CN城市污水与硝酸盐废水的运行特性杜世明
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