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当前位置:首页 > 商业/管理/HR > 企业文化 > UASB接触氧化处理高浓度有机废水试验研究汤立炯
UASB-1 2(1.上海市机电设计研究院,上海 2000040;2.华东师范大学环境科学系,上海 200062) UASB+,UASB。CODcrUASB,。 UASB StudyonTreatmentofHighConcentrationOrganicWastewaterbyUASBReactorandContactAeratorTangLijiong1 ZhangMin2(1.ShanghaiInstituteofMechanicalandElectricalEnginecring Shanghai 200040;2.DepartmentofEnvironmentScience,EastChinaNormalUniversity Shanghai 200062)Abstract UASBreactorandcontactaeratorwereusedtotreatwastewaterofchemicalplant.Onthebasisofmea-suringandanalyzing,discussedthepossibilityofuseUASBtotreathighconcentrationorganicwastewater.Besides,theeffectofCODcrvalueandsaltconcentrationtoUASBtreatmenteffectefficiencyandselectionofitskeyparameterswerealsodiscussed.Keywords UASB contactaerator anaerobic aerobic organicwastewater1 ,CODcr、BOD,,CMC,(CODcr50000mg/L),(6%);,。,UASB+。UASB(UpflowAnaerobicSludgeBlanket),WageningenLettinga1972,(1);(2);(3)(、、)。,,,。,。2 2.1 CMC,CODcr42640mg/L,BOD520700mg/L,pH6.1,()5.54%。,pH7.5,30℃,N、P[1](C∶N∶P=200∶5∶1)。 (3)Y280,。1 ,,,2000,3。:,1974,,,。22 WATERPURIFICATIONTECHNOLOGYDOI:10.15890/j.cnki.jsjs.2002.03.008 ,N、P(C∶N∶P=100∶5∶1)。2.2 2.2.1 CMCCMC1,15L。1 UASB,,,AF。,,。2.2.2 2,15L。2 2.3 :CODcr、BOD5、、pH[2]。3 3.1 CMC3.1.1 ,CMC,,,,CMC,1。1,,CODcr4028mg/L5137mg/L,0.5%0.8%,2.873.696,CODcr41%49.6%,UASB,,,。1 驯化过程进出水水质情况(d)CODcr(mg/L)(%)(kgCOD/m3d)CODcr(mg/L)(%)140280.52.87——540280.52.87237641.0651370.83.696——1051370.83.696259049.62 UASB装置运行参数(d) CODcr(mg/L)(%)(kgCOD/m3/d)CODcr(mg/L)CODcr(%)053360.73.69——153200.73.69305442.6253150.73.67291845.1362910.85.25298252.6462800.85.24305851.3562610.85.23291853.4663370.85.27287754.6763921.15.28280056.2886201.16.48348259.6986791.16.46388055.31087271.16.49370957.51186891.17.56374556.91487601.17.54353959.61586711.17.55345160.21786381.17.49331761.619106001.49.1497153.120105401.49.1626140.621104501.49.1709632.122106001.49.1810923.53.1.2 CMCCMC,pH,N、P,23 Vol.21NO.32002 ,HRT24h。2。,CMC,CMC。,CMC8,CODcr40%。,85,,CODcr5330mg/L8638mg/L,0.7%1.1%,3.69kgCODcr/m3d7.5kgCODcr/m3d,,CODcr(40%60%)。,7.5kgCODcr/m3d,CMC5,UASB,CMCCODcr60%。CODcr,CODcr10000mg/L,1.4%,。,。,CMCUASB,7.5kgCODcr/m3d,1.1%。CMC,CODcr60%。3.2 ,CMCUASB5,N、P,HRT15h,3。3 好氧处理模型试验结果(mg/L)(mg/L)%CODcr:93714698*84.489.5*BOD5:35228*92.0* *:3,CMC(CODcr:937mg/L,BOD5:352mg/L),,CODcr150mg/L,100mg/L,BOD530mg/L。4 4.1 CMCUASB。,CODcr60%。1.1%,7.5kgCODcr/m3d。4.2 CMCUASB,,CODcr150mg/L,,(),CODcr100mg/L,BOD530mg/L。1 .《》.,19982 ..,《》,:,19983 .《》.,2000,9,P333:,19695,,,、。———2003《》———《》1975,,、、、、、、、、、、、,、、、、、、。《》,“”,,SCI、CA。《》,28,16,64,,8/,:32-38,,。《》,。:50 :310012 :(0571)88866168-2161 :(0571)8891202124UASB-
本文标题:UASB接触氧化处理高浓度有机废水试验研究汤立炯
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