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当前位置:首页 > 商业/管理/HR > 质量控制/管理 > 附加回流的生物接触氧化工艺净化滇池大清河水质的示范工程研究张辉
3 2环境工程学报Vol.3,No.220092ChineseJournalofEnvironmentalEngineeringFeb.2009张 辉 温东辉* 李 璐 谢曙光(,100871) ,(IBCOP)。IBCOP1000m3/d,HRT4.75h,20071120084,,3。:CODNH+4-N,46.8%48.8%,NH+4-N;、、DO,TN,10.2%,;,TP17.9%,TP、。 (IBCOP) X703.1 A 1673-9108(2009)02-0199-06Demonstrationworkofinter-cyclebiologicalcontactoxidationprocessforpurificationofDaqingRiverinDianchiLakewatershedZhangHui WenDonghui LiLu XieShuguang(CollegeofEnvironmentalSciencesandEngineering,PekingUniversity,Beijing100871)Abstract DaqingRiveristhemostseriouslypollutedriverintheDianchiLakewatershed.Abypassdem-onstrationworkoftheinter-cyclebiologicalcontactoxidationprocess(IBCOP),withthetreatmentscaleof1000m3/dandtheHRTof4.75h,wasbuiltaroundtheriverbanktopurifytheriverwater.DuringthewinterdryseasonfromNov.2007toApr.2008,threesetsofconditionsofthedemonstrationworkwereoperatedbyregula-tingcyclingratiobasedontheinfluentqualitiesandclimaticconditions.TheresultsshowedthattheIBCOPdem-onstrationworkkeptbetterremovalefficienciesforCODandNH+4-N,andtheaverageremovalrateswere46.8%and48.8%respectively.Thehighercyclingratio(150%)wasfavorableforremovalofNH+4-N.TheaverageremovalrateofTNwasloweras10.2%,owingtothenegativeimpactsoflowtemperature,carbonsourceshort-age,higherDOleveloftheinfluent,andlooseandporousbiofilm,regulatingcyclingratiocouldnotimprovetheconditionofcarbonsourceshortageremarkably.TheabsorptionbySpirogyrasp.anddepositionofsludgewerethemaincausesofTPremovalandtheaverageremovalrateofTPwas17.9%,lowTPconcentrationofinfluent,detachmentofbiofilmandhighercyclingratioweredetrimentalforTPremoval.Keywords inter-cyclebiologicalcontactoxidationprocess(IBCOP);riverwater;removalrate;demon-strationwork;DianchiLakewatershed:(863)(2005AA601010-03);(50778001):2008-06-18;:2008-08-11:(1983~),,,。E-mail:1983ahui@163.com*,E-mail:dhwen@pku.edu.cn ,,2920km2,5.7m3[1],15.6m3。,。,45%~56%,2005COD、TNTP62.9%、75.5%65.8%[2]。29,,。3,,,、、,()。7.8×107m3,,50%。、NH+4-N,,、、[3~6]。-(anoxic-aerobic,A/O),,,,,。A/O,,。A/O,(in-ter-recyclebiologicalcontactoxidationprocess,IB-COP),,IBCOP。1 1.1 IBCOP,30m×3m×3m,2.2m,1000m3/d,HRT4.75h。A/O,1∶3,SHX,SHX,。,。,225m2,1.5m,。IBCOP(),;,。IBCOP1。1 IBCOPFig.1 SchematicofIBCOPdemonstrationwork1.2 IBCOP200711,20084。,,1。,,。,;,,。6IBCOP,3,:、。:TN、NH+4-NTP,NO-3-N;TN、NH+4-NTP,NO-3-N;TN、NH+4-NTP()(),NO-3-N;COD,,;。2002 :pH,8.17;,15.8℃,3,18.2℃;,0mg/L,,6mg/L,,2.5mg/L。IBCOP3,2。1 Table1 WatertpropertiesofDaqingRiverpH(℃)COD(mg/L)BOD5(mg/L)TP(mg/L)TN(mg/L)TKN(mg/L)NH+4-N(mg/L)//70~11030~501.5~1.722~2520~2415~207.801590401.623.522182 IBCOPTable2 ParametersandinfluentconditionsoftheIBCOPdemonstrationworkHRT(h)(%)pHDO(mg/L)(℃)COD(mg/L)TN(mg/L)TP(mg/L)1a4.753∶11007.46~7.890.05~6.7913.9~15.818.04~78.932.12~23.770.04~1.952-1b4.753∶1757.69~8.791.81~14.6913.5~14.423.58~57.896.78~19.230.21~1.352-2c4.753∶1757.51~8.270.08~11.4915.4~17.835.56~133.6020.99~23.771.34~1.863d4.753∶11508.26~8.5910.6~12.9816.2~20.131.32~56.223.80~20.700.30~1.04 :2-12-22,,;a:12007.11.25~2007.12.13;b:2-12007.12.15~2007.01.08;c:2-22008.03.08~2008.03.23;d:32008.03.25~2008.04.161.3 COD:;TN:-;TP:;NO-3-N:;NH+4-N:;DO、pH:MettlerToledoDOpH。2 IBCOPCOD、TP、TN、NH+4-NNO-3-N3,。2.1 1,IBCOP,,。COD、TP、TNNH+4-N36.0%、21.5%、11.7%40.6%。1IBCOP,;,,,IBCOP,,。1IBCOP(Spirogyrasp.),。,,,,TP、TNCOD[7~9]。,,,,。20133 IBCOPTable3 WaterqualitiesofeffluentoftheIBCOPdemonstrationwork 12-12-23pH7.71~8.147.62~8.017.59~7.687.54~7.78DO(mg/L)5.3~7.753.55~8.212.66~4.133.83~6.07(℃)13.4~16.013.0~14.015.0~17.415.4~19.4(%)36.051.349.246.9COD(mg/L)32.6719.5637.2020.03(mg/L)14.33~44.448.89~43.4214.68~55.465.91~31.73(%)21.516.318.7-18.7TPa(mg/L)0.820.511.310.62(mg/L)0.10~1.440.19~1.141.19~1.420.39~0.96(%)11.710.98.110.4TN(mg/L)10.7011.8020.718.72(mg/L)2.21~18.836.04~17.4119.62~21.673.12~18.66(%)40.663.415.569.8NH+4-N(mg/L)9.623.6819.193.27(mg/L)0.11~19.090.46~12.0914.39~23.970.17~10.24 :a12TP;3TP 1COD,18.04mg/L,25.55mg/L,,,,COD;,IBCOPCOD36%,68.2%。IBCOP,TP。1TP,0.04mg/L,,;TP,,,IBCOPTP17.5%~26.2%。1TN,2.12mg/L,,,,IBCOP,TN;,TN,,,IBCOPTN5.4%~24.9%,11.7%。,13.9~15.8℃,14.4℃,,TN[10,11];COD/TN2.9,。1,NH+4-N,,IBCOPNH+4-N53.4%~88.4%。NH+4-N,IBCOPNH+4-N,10.9%~29.4%。,:NH+4-N,0.08~0.12kg/(m3·d);NH+4-N[12,13],100%,,NH+4-N。1,,NH+4-NTN,,COD/TN。,,NH+4-N,,COD2022 :。2.2 22-1,,,IBCOP,,,,;2-2,,,,,,。IBCOP2COD、TP、TNNH+4-N50.3%、17.4%、9.7%43.2%。2-1COD,75%,COD,,IBCOPCOD51.3%。2-1COD,45.01mg/L,60.9%~80.8%;COD36.50mg/L,30.24~57.89mg/L,,,14.1%~31.8%。2-2COD,74.80mg/L,,35.56~133.60mg/L,,27.5%~74.2%,49.2%。2-12-2,IBCOP,1,,,,,1。2-1:IBCOPTN,0.7%~30.2%,10.9%。,7mg/L,,,CODNH+4-N,;COD/TN1.82~6.27,NO-3-N,,75%。2-2TN,20.99~23.77mg/L,TN,8.1%。,,6mg/L,TN;COD/TN1.6~5.6,NO-3-N,。2NH+4-N1,NH+4-N,;NH+4-N,。2-1NH+4-N1,,,75%,IBCOPNH+4-N30%,NH+4-N,82.4%。2-2,NH+4-N,25.76mg/L,0mg/L,,NH+4-N,,2.4%。NH+4-N[13,14],,,28%。2.3 3,,。,IBCOP,,,,。COD、TP、TNNH+4-N46.9%、-18.7%、10.4%69.8%。3COD31.32~56.22mg/L,150%COD,,IBCOPCOD,46.9%。,,,,,,,,,12.1%~85.0%。3TP,,TP,。,,,;,。,,,TP。3TN0.4%~19.2%,10.4%,,COD/TN,;8mg/L,,;,2033,,[15],。3NH+4-N69.8%,93.5%。NH+4-N9mg/L,54.4%;NH+4-N9mg/L,83.1%;NH+4-N2mg/L,NH+4-N。(150%)NH+4-N,NH+4-N。3,NO-3-N,NH+4-N,,,。3 IBCOP,,,、,:(
本文标题:附加回流的生物接触氧化工艺净化滇池大清河水质的示范工程研究张辉
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