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当前位置:首页 > 建筑/环境 > 工程监理 > 广州新塘某印染工业园污水处理与资源化设计易皓虢清伟李小虎许振成
51065510×104m3/d“+”CEAO“//”。《》GB4287—2012。、。CEAOX703C1000-4602201402-0034-04DesignCharacteristicsofWastewaterTreatmentandReutilizationinaPrintingandDyeingIndustrialParkinXintangTownofGuangzhouCityYIHaoGUOQing-weiLIXiao-huXUZhen-chengSouthChinaInstituteofEnvironmentalSciencesMEPGuangzhou510655ChinaAbstractThewastewatertreatmentplantinaprintinganddyeingindustrialparkinXintangTownofGuangzhouCitywasexpandedwiththecapacityof10×104m3/d.Thehydrolyticacidification/aerobicprocesscombinedwithselectivephysico-chemicaltreatmentprocessChinaEverAnaerobicOxidationprocesswereapplied.Sludgeheatpumpdryingandincinerationtechnologyandtailwaterrecoveryprocesswithacombinationofcoagulationsedimentationfiltrationanddisinfectionwerealsoapplied.AfterstableoperationofthesystemwasachievedtheeffluentqualitycouldmeetDischargeStandardofWaterPollutantsforDyeingandFinishingofTextileIndustryGB4287-2012.Treatedsludgeandtailwatercouldbereutilized.Thetreatmentprocessflowthedesignparametersofdifferentunitsandtheprocesscharacteristicswereintroducedtoprovidereferenceforothersimilarprojects.KeywordsCEAOprocesssludgereutilizationtailwaterreusedesigncharacteristic2012ZX07211-003。、。《》GB4287—2012。·43·30220141CHINAWATER&WASTEWATERVol.30No.2Jan.2014160005×104m3/d2.877hm2+A/O。2004200610×104m34~5×104m3。200810×104m3/d。22.1、19。、、1。、2。《》GB4287—92。《》GB4287—20121。、1。1、Tab.1DesigninfluentandeffluentqualityaswellasrevisedeffluentqualityCOD/mg·L-1BOD5/mg·L-1SS/mg·L-1/pH/mg·L-1600~1200177~400580~880355~5309~122~10≤100≤25≤70≤406~9≤1.0≤100≤25≤60≤706~9≤1.02.2CEAO“+”AO、。1。1Fig.1Flowchartofwastewatertreatmentprocess33.1、、。①30150m3/h。2t/d。。、。、、。。。。a.。。b.。。②118.0·53·.watergasheat.com302m×15.0m×6.0m0.8h。。。。pH9~12pH9~10.5COD。pH。。3.2①623.0m×21.0m×7.5m10h2kgCOD/m3·d。PVA。20063“-”。②263.0m×27.0m×6.5m10h4kgCOD/m3·d8∶1。、、、、。2006CEAO。、。。③5、136.0m×4.5m430.0m×4.5m。PACPAMCOD。3.3、40%。2。2Fig.2Flowchartofsludgetreatmentprocess。。。8.37~12.5MJ10.46MJ14.65MJ71%、27.2MJ38.4%4。“”·63·302.watergasheat.com。3.410×104m3/d7~8×104m3/d1.2~1.5×104m3/d1∶4。3。3Fig.3Flowchartofwastewaterreclamationsystem4《》GB4287—20121。、2。2、Tab.2ActualinfluentandeffluentqualityCOD/mg·L-1BOD5/mg·L-1SS/mg·L-1/pH/mg·L-1500~700210~330420~560230~4009~123~540~6010~2045~5540~607~7.50.3~0.560000.593kW·h/m30.40/m30.017/m31.01/m31.00/kW·h。5CEAO、。、30%、。1.//J.2008241756-58.2.J.2007429-31.3.J.2004301248-51.4.J.201241117-21.1982-。E-mailyihao@scies.org2013-08-07·73·.watergasheat.com302
本文标题:广州新塘某印染工业园污水处理与资源化设计易皓虢清伟李小虎许振成
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