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CHEMICALINDUSTRYANDENGINEERINGPROGRESS20153451444121211·113100362310036anaerobicammoniumoxidationAnammoxX703.1A10006613201505144410DOI10.16085/j.issn.1000-6613.2015.05.043AdvancesinapplicationsofAnammoxprocessZHANGZhengzhe12JINRencun12CHENGYafei1ZHOUYuhuang1BUAYIXiemuguli11CollegeofLifeandEnvironmentalSciencesHangzhouNormalUniversityHangzhou310036ZhejiangChina2KeyLaboratoryofHangzhouCityforEcosystemProtectionandRestorationHangzhouNormalUniversityHangzhou310036ZhejiangChinaAbstractAnaerobicammoniumoxidationAnammoxhasadvantagesofhighefficiencyandlowconsumption.Thismethodhasbecomeapromisingbiologicalnitrogeneliminationprocess.Thispapercomparedtheoperationconditionsofone-andtwo-stageAnammoxprocessesanalyzedthehabitatandspeciesdiversityofanaerobicammoniumoxidizingbacteriaandprocessversatilityofAnammoxandsummarizedthelaboratoryresearchandengineeringapplicationsofAnammoxinthetreatmentofvarioustypesofammonium-richwastewater.Thecharacteristicsresearchprogressandapplicationbarriersofsludgedigestaterejectwaterlandfillleachatelivestockwastewatermunicipalsewagesalinewastewateretcwereintroduced.MoreoverthepotentialproblemsofAnammoxprocessinpracticalapplicationswerediscussedandfurtherresearchfocusesweresuggested.KeywordsAnammoxcombinedprocessactualwastewaterbiologicalnitrogenremovalengineeringapplicationsanaerobicammoniumoxidationAnammox[1-2]2014-09-262014-10-19510781215127816220091133B062014103460171991—E-mailzhangzhengzhe@126.comE-mailjrczju@aliyun.com51445anaerobicammoniumoxidizingbacteriaAnAOB11[m(VSS)/m(NH4+-N)=0.11g/g[3]AnAOBAnAOB1AnAOB6181AnammoxaceaeAnAOB[4][5][6][7][8][9][10][11][12]AnAOB2CANONcompletelyautotrophicnitrogenremovalovernitriteOLANDoxygenlimitedautotrophicnitrificationanddenitrificationDEAMOXdenitrifyingammoniumoxidationDEMONaerobicdeammonificationSNAPsimultaneouspartialnitrificationanammoxanddenitrificationSNADsingle-stagenitrogenremovalusinganammoxandpartialnitritationSHARONsinglereactorforhighactivityammoniaremovalovernitrite-anammox21AnAOBBrocadiaCandidatusBrocadiaanammoxidans[13]CandidatusBrocadiafulgida[14]CandidatusBrocadiasinica[15]CandidatusBrocadiabrasiliensis[16]CandidatusBrocadiacaroliniensis[17]KueneniaCandidatusKueneniastuttgartiensis[18]ScalinduaCandidatusScalinduasinooifield[6]CandidatusScalinduazhenghei[19]CandidatusScalinduarichardsii[20]CandidatusScalinduabrodae[21]CandidatusScalinduawagneri[21]CandidatusScalinduasorokinii[7]CandidatusScalinduaarabica[22]CandidatusScalinduaprofunda[23]AnammoxoglobusCandidatusAnammoxoglobuspropionicus[24]CandidatusAnammoxoglobussulfate[25]JetteniaCandidatusJetteniaasiatica[26]AnammoximicrobiumCandidatusAnammoximicrobiummoscowii[27]2NOBpH“2015341446”32014100[28]33.1pH7.08.53037AnAOBvanDongen[35]-Dokhaven80%Fux[36]3/m3/d/kgNH4+-N·m−3·d−1/kgN·m−3·d−1DEMONStrassSBR5009000.680.6[29]DEMONGlamerlandSBR400500.630.4[30]CANONOlburgenUBR+6001802.081.3[31]CANONZürichSBR+14001800.45—[1]CANONSt.GallenSBR+3001500.36—[1]CANONNiederglattSBR+160900.35—[1]ANAMMOX®6700301.67[28]ANAMMOX®5002.00[28]OLANDPitesaRBC24090-150—1.7[7]OLANDSneekRBC—6——0.9[28]SHARON-ANAMMOX®RotterdamUBR+1500+701260—9.5[32]SHARON-ANAMMOX®UASB+300+5886—1.043.29[33]CIRCOX-ANAMMOX®LichtenvoordeABR—150+75——1.71.9[28]SHARON-ANAMMOX®Mie3600+58603[34]ABRair-liftbioreactorMBBRmovingbedbiofilmreactorRBCrotatingbiologicalcontactorSBRsequencingbatchreactorUBRup-flowbioreactorUASBup-flowanaerobicsludgeblanket51447-1600LsequencingbatchreactorSBR620650mg/LpH7.37.52628nitrogenloadingrateNLR0.65kgN/(m3·d)nitrogenremovalefficiencyNRE92%[36]2002-Dokhaven70m3750kgN/d[32]75%[28]3.23000mg/L5002000mg/L10000mg/L[37]Liang[38-39]“--”166COD97%87%89%Liu[40]-7093%-[41-42][43][38]3.3COD[44]-Hwang[45]SHARON-1.26SBRup-flowanaerobicsludgeblanketUASBN213mg/L323mg/L92mg/L77mg/LYamamoto[46]SHARON-220NREnitrogenremovalrateNRR55%0.22kg/(m3·d)[46]NRRAnAOB3.4CODbiochemicaloxygendemandBODNH4+-NSO42−pH2[47][48]71NRR0.457kg/(m3·d)Shen[49]AnAOB3600.11kg/(kgVSS·d)0.09kg/(kgVSS·d)0.16kg/(kgVSS·d)20153414486600m350005500mg/LAnAOB+-+-3.5[50]Toh[50]AnAOB50mg/L500mg/L15NRR0.062kg/(m3·d)NRR1.5AnAOB320330mg/LNRR0.12kg/(m3·d)[51][52]3.623W6W0.8W[53][54]815Hu[55]-25SBR5L1012300NRE90%[56]359.1NRR6.61kg/(m3·d)Lotti[57]AnAOB10204m319±1[58]ammonia-oxidizingbacteriaAOBAnAOBnitrite-oxidizingbacteriaNOB3.7Vlaeminck[59]OLAND2.50.7kg/(m3·d)NRE76%deGraaff[60]-39mg/LNRR0.5kg/(m3·d)NRE87%N2ON2OdeGraaff[61]-Sliekers[62]CANONSBRAOBAnAOBAnAOBAOBLiu[63]AnAOB-51449[64]3.8[65]Dapena-Mora[66]SHARON-7001000mg/L800010000mgNaCl/LNLR0.5kg/(m3·d)68%SHARONNO2−-N/NH4+-N1110gNaCl/L[65]30gNaCl/L3075gNaCl/L[67][68]3.94Tang[69]-10mg/L510mL0.30.6gVSS0.025gVSS/(L·d)NRR9.4kg/(m3·d)50mg/LChen[70]COD194577.8mg/LNRE85%COD56.6%Tokutomi[33]---10NRR1.043.29kg/(m3·d)260450mg/L8mg/L-Daverey[71]CANON18LSBRNaHCO3850mgCaCO3/L3636mg/LNLR0.909kg/(m3·d)98%1737CANON4120153414504/LHRT//pH/kg·m−3·d−1/%C/NRBC50RBC1147.850.4242[72]MBR1.50.751.120300.5582[73]SBR160030.431.87.457.590.560.648599[36]SBR1119217.50.0869[74]SBR1013037780.550.95[35]SBR31.8357.58.20.34080[66]CODSSCSTR0.730.2307.52.6077[75]U
本文标题:厌氧氨氧化工艺的应用进展
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