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ComparisonoftwokindsofaminoacidwastewatertreatmentprocessesWangXiaoxia,QiuZhaofu,LinZhe,WuSheng,GuYinyu,LüShuguang(CollegeofResourceandEnvironmentalEngineering,EastChinaUniversityofScienceandTechnology,Shanghai200237,China),,,,,(,200237)[],。,,COD0.39~1.00kg/(m3·d)、TN0.05~0.16kg/(m3·d),CODTN,COD100mg/L、NH4+-N1~3mg/L。,、SS、。[];;;[]X703.1[]A[]1005-829X(2009)02-0026-03Abstract:Thetreatmenteffectofaminoacidwastewaterbytwokindsofbiologicaldenitrificationmethods,activat-edsludgeandbiofilmprocesseshavebeeninvestigated.Theresultsshowthatbothprocessesperformwellwithef-fluentCOD100mg/Landeffluentammonianitrogenintherangeof1-3mg/LunderthesameorganicandnitrogenloadsCOD0.39-1.0kg/(m3·d),TN0.05-0.16kg/(m3·d).Biofilmprocessexhibitsalittlebitbetterinorganismre-movalrateandsystemstability,andisbettersignificantlyinsludgeproduction,effluentSSandshockloading.Keywords:denitrification;aminoacidwastewater;biofilmprocess;activatedsludgeprocess:、,〔1〕;〔2〕,。、〔3-5〕。,,,。11.1、。COD500~2000mg/L、TN70~300mg/L、pH8.4~8.7、B/C0.6~0.7。5,,COD/TN。1.2—,A/O。2A/O,(A)(B)。A、B1。A、B,1,BZV-150-60,29220092IndustrialWaterTreatmentVol.29No.2Feb.,2009261(A)(O)HRT/h108242/L54121。,0.5L/h,30℃,R=3,r=1(A)。(O):pH7.5,DO>2mg/L。1.3COD、BOD5、、、、、MLSS,〔6〕。ORP、pH、DO、。22.1,A、B、SS2。2,COD490~2000mg/L,COD50~100mg/L,COD90%~97%。COD,COD。,NH4+-N,。TN70~230mg/L,TN,NH4+-N,1~3mg/L;ATNB,B〔7〕。TN296mg/L,NH4+-N,20mg/L。,NH4+-N15mg/L,TN≤226mg/L。2,COD,BSSA。A、B,。,COD1450mg/L、TN226mg/L,A、B,CODNH4+-NGB8978—1996。2.2COD、TN2、3。2,COD0.39kg/(m3·d)1.37kg/(m3·d),A、BCOD,BA,,B,COD。3,TN0.05kg/(m3·d)0.12kg/(m3·d),TN75%97%;TN0.12kg/(m3·d),TN97%82%。TN0.12kg/(m3·d)。,TN,0.12kg/(m3·d),ATNB,2。2.3BOD4。4,A、BBOD,0.1652、,:2009-02,29(2)2A、BCODNH4+-NTNSS493070.0—A441.3210.265B472.1622.6357470109.0—A412.1210.885B342.3324.6389880148.0—A690.888.7102B301.3616.24514500226.0—A511.4219.3105B382.5421.85819860296.0—A8518.6439.9110B8019.9646.765mg/L270.0178,A、B0.1652、0.0178kg/kg。,BA,〔3〕。1/4〔8〕,BA1/9,B。2.4,7d,5、6。,3dTN0.15kg/(m3·d),4TN0.38kg/(m3·d),5TN0.15kg/(m3·d)。5、6,A、B,。B2d,3d,BA,COD。。ASVI3。3,,ASVI,,。3(1)COD0.39~1.00kg/(m3·d)TN0.05~0.16kg/(m3·d),CODTN,COD<100mg/L、NH4+-N1~3mg/L。(2)、,、SS。(3),,,。[][1],.[M].:,2000:50-51.[2].[J].,2000,26(2):37-39.[3],,.[J].:,2001,27(2):205-209.[4],,,.NH4+-N[J].:,2005,19(2):42-45.[5],,.MBBR[J].,2005,15(6):336-338.[6].[M].4.:,1997:105-284.[7],.[M].:,1998:118-119.[8],.[M].4.:,1999:201.[](1973—),1996,。:021-64253132,E-mail:xxwang@ecust.edu.cn。[]2008-08-052009-02,29(2)3ASVISVI/(mL·g-1)9811214620421628
本文标题:氨基酸废水的两种处理工艺比较王晓霞
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