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1111222131.1001242.0210003.150090。3~4℃。、。、、。TU991A1000-4602201511-0001-0451222807NCET-10-0008E-maillidong2006@mail.bjut.edu.cnAnalysisonReasonsofStandard-exceedingofWaterQualityinWaterworksandItsSolutionsMENXuan1LIDong1CAIYan-an1ZENGHui-ping1LIYuan-bin2SUNHai-lin2LIShu-qi2ZHANGJie131.KeyLaboratoryofBeijingforWaterQualityScienceandWaterEnvironmentRecoveryEngineeringBeijingUniversityofTechnologyBeijing100124China2.HailarDistrictWaterSupplyCompanyHulunbeir021000China3.StateKeyLaboratoryofUrbanWaterResourceandEnvironmentHarbinInstituteofTechnologyHarbin150090ChinaAbstractReasonsofstandard-exceedingofwaterqualityinmanganeseremovalwereinvestigatedbasedontheoperationaldataofawaterworks.Theanalyticalresultsindicatedthatpotassiumpermanga-nateasastrongeroxidantfailedtoachievemanganeseoxidationinlow-temperaturegroundwater3to4℃insteadcausedahighermanganeselevelintheproducedwaterthanthatinrawwater.Thesolu-tionwasusingliquidchlorineasoxidantandthechlorinewasdosedattheinletofthefilterfollowingtheairfloatationtank.Theresultsshowedthatthechlorinationcouldachievethesimultaneousremovalofi-ronmanganeseandammonianitrogen.Thenormaloperationoftheairfloatationtankcouldeffectivelya-voidthegenerationofdisinfectionby-productsinthechlorinationprocess.Keywordslow-temperaturegroundwaterFeandMnremovalpotassiumpermanganateoxi-·1·311120156CHINAWATER&WASTEWATERVol.31No.11Jun.2015dationbreak-pointchlorination、。3~4℃《》。。1、、2.8~3.2、0.38~0.45、0.90~1.20mg/L。1。A、B。。1Fig.1Watertreatmentprocessusedinwatersupplyplant。。、、。。、。、、。。。。2<0.5mg/L0.1mg/L<0.3mg/L。1。。1450m3/h1。ⅠⅡ4~5mg/LⅢⅣ。1Tab.1Waysforapplicationofreagentsindifferentperiodspriortorunningtestsmg·L-1Ⅰ25~30——Ⅱ25~301—Ⅲ25~30—6~8Ⅳ25~300.3~0.56~82.1Ⅰ。。A、B0.3mg/L。·2·3111.watergasheat.com0.5mg/L。<0.1mg/L。820mV200mV。。。1。220mV。。2.2Ⅱ、、2。2ⅡFig.2WatertreatmenteffectsduringoperationalperiodⅡ1mg/LⅠ。。A、B0.6、0.7mg/L0.6mg/L0.4mg/L0.2mg/L。1mg/L0.35mg/L0.2mg/L0.57mg/L0.43mg/L。。1mg/L0.94mg/L。2.5mg/L2.35mg/L。1mg/L0.43mg/L。。。2.3Ⅲ、3。3ⅢFig.3WatertreatmenteffectsduringoperationalperiodⅢ30.5mg/L。。。。。2.41mg/L8mg/LⅣ>1mg/L。·3·.watergasheat.com311120.3~0.5mg/L。43~4℃。4ⅣFig.4WatertreatmenteffectsduringoperationalperiodⅣ3①②。。—。、1。3。、。0.06mg/L0.13mg/L。—。4①、、。、、。②—。③。④、、。1.J.201130860-64.2.J.20077557-59.3.J.201430131-5.1990-。E-mailmenxuan90@126.com2015-02-28·4·3111.watergasheat.com
本文标题:供水厂水质超标问题诊断与调试运行思路
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