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ABRSBRρ(CODCr)/(mg·L-1)2000ρ(BOD5)/(mg·L-1)700ρ(SS)/(mg·L-1)300/200/(m3·d-1)200pH5~6.5ABR-SBR1,2,2(1.,545000;2.,530022):—(ABR-SBR)。,CODCr438~2300mg/L,BOD5310~824mg/L,SS86~229mg/L50~220,GB21906—2008《》,、、。:;;;:X7:B:1674-4829(2010)02-0023-020。、,,。,ABR-SBR。,,CODCr,BOD5,SS,GB21906—2008《》。11.1、、、。,、、、、、、、,[1]。、1。1GB21906—2008《》。1.2、,ABR-SBR,1。1ABR;ABRCOD,ρ(BOD)/ρ(COD)0.4;,SBR。ABR,:2010-02-26:(1978-),,,,,.、.ApplicationofABR-SBRProcessinTreatmentofWastewaterfromProductionofPreparedTraditionalChineseMedicineLIHong-hua,DENGHai-tao,YAOBingAbstract:Anaerobicbaffledreactorandsequencingbatchreactor(ABR+SBR)processwasusedinthetreatmentofthewastewaterfromtheproductionofpreparedtraditionalChinesemedicine.TheresultsofoperationshowedthatwhentheCODCrwas438~2300mg/L,BOD5was310~824mg/L,SSwas86~229mg/Landchromawas50~220timesintheinletwater,respectively,theoutletafterthetreatmentreachedGB21906-2008.Theprocesshasthemeritsofsimpleoperation,strongshockloadcapabilityandlowoperationcost.Keywords:Anaerobicbaffledreactor(ABR);Sequencingbatchreactor(SBR);TraditionalChinesemedicine;Wastewatertreatment23220104EnvironmentalScienceandTechnologyVol.23No.2Apr.201020104。1.31.3.1ABR(AnaerobicBaffledReactorABR)MCCARTY。,[2]。ABR。,。ABR,,。1,,,,。ABR,[3-4]。,ABR4,5m×5m×4.5m(××),0.5m,100m3。ABRHRT=48h,34150mm×80mm60m3,2:①,;②,ABR[5]。1.3.2。5m×5m×5m(××),112.5m3,HRT=13.5h。80WQ50-10-32,11,50m3/h,10m,3kW。1.3.3SBRSBR,1,[6]。SBR、。8m×5m×5.5m(××),200m3,HRT=24h。SBR5、、、(),1。112h,,2h,1h,4h,1h,2h,2h。2,100m3。,150WQ145-9-7.52,11,145m3/h,9m,7.5kW。12,3.3m2。,1.81。,,SBR,,。SBR,,、、。1.3.42,3m3,。ABR1。2200810,,2,,。12,2d,4,2。2,GB21906—2008《》。352,30,22。0.25。、,。4(1),ρ(CODCr),ρ(BOD5),ρ(SS),1440mg/L,560mg/L,180mg/L,156,14mg/L,6mg/L,23mg/L,10;99%,98.9%,87.2%,93.5%,。(2)ABR4,3,4,ABR,,。(3)ABR-SBR,、、,GB21906—2008《》。(27)ABRSBR5.34~9.876.71~7.027.25~7.696~9ρ(CODCr)/(mg·L-1)438~2300223~27810~23100ρ(BOD5)/(mg·L-1)310~824110~1554~720ρ(SS)/(mg·L-1)86~22925~3615~2950/50~22025~408~1550pH224232!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!!![][1],.-(ABR)-[J].,2007,20(2):43-44.[2],,.·[M].:,2000.[3],.ABR[J].,2008,21(4):33-35.[4],.-[M].2.:,2006.[5],,.--ABR-SBR[J].,2007,20(4):37-38.[6].[M].:,2003.(),0.3m/s,,,。,,,MLSS4000~5000mg/L。1#,2#,()。2,1.5~2.5mg/L。6、2008,,。2。,GB18918—2002《》A。7(1)。,,、、,。(2),,,。8,,,,,GB18918—2002《》A。。[][1],,,.[M].:,1997.[2],.[M].:,2005.[3],.[J].,2008,21(2):64-66.[4].[J].,2008,21(4):72-74.()2、ρ(CODCr)ρ(BOD5)ρ(SS)ρ(TN)ρ(NH3-N)ρ(TP)54564.537.219419.58.7537033.917.251.74.1534.122.83.475.340.32mg·L-1(24)##############################################27
本文标题:ABRSBR工艺处理中成药制药废水李红华
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