含高浓度硝酸根废水的处理研究白延利

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405201810GANSUMETALLURGYVol.40No.5Oct.20181672-4461201805-0041-04*11121131.7301012.7301013.730000、、、、、、II、III、NO-35000~30000mg/L。NO3-≤15mg/L《、》。X703AStudyontheTreatmentofWasteWaterwithHighConcentrationofNitrateBAIYan-li1ZHANGJing1LIUGuo-qi1ZHANGZong-lei2RENZhi-yong1WANGHong-mei1CHENFeng-juan31.LanzhouJinchuanPreciousMetalMaterialsCo.Ltd.Lanzhou730101China2.GansuJingpuDetectionTechnologyCo.Ltd.Lanzhou730101China3.LanzhouUniversityLanzhou730000ChinaAbstractPalladiumnitrateplatinumnitraterhodiumnitratedinitrodiamineplatinumdinitrodiaminepalladiumdiam-minetetraamminepalladiumtetranitroplatinumIIpotassiumandnitrosylnitrateIIIplayanimportantroleWhenusedasprecursorsforhomogeneouscatalystsormultiphasecatalystsinthefieldsofmedicinechemicalengineeringetc..Dur-ingtheproductionoftheseproductswastewatercontaininghighconcentrationsofnitratesisproduced.TheNO3-contentofthewastewateris5000~30000mg/L.Inthispaperthetreatmentofnitrateinthecompany'shigh-concentrationwastewaterwasstudied.Thenitratereductioninthewastewaterwasdeterminedbythechemicalmethod.Theresultsshowthatthemethodcanremovenitrateinthewastewatereffectivelyandthecostislow.Itissuitableforlarge-scaleapplica-tion.Thecontentofnitrateofthetreatedwastewaterisbelow15mg/LfulfillstheeffluentrequirementsofIndustryPollutantEmissionStandardoftheCopperNickelandcobalt.KeyWordshighconcentrationnitratewastewaterchemicalreduction1。、。NO-3FeⅡFeⅢ。、。。《、》NO3-15mg/L40mg/L。。*《》1203GKDA014。DOI:10.16042/j.cnki.cn62-1053/tf.2018.05.014、、、、、、II、III、NO3-5000~30000mg/L300t。。、、、、、。Rivett1-2pHCu。Wang3-5。50mg/L25mg/L。。Shin618~25mg/L1000h65%。。Wang7。10℃pH6~8。、。NO3-Cl-HCO3-8-9。BODCOD。、、。22.11。2.22。2.3NO3-。1。111200g22100g33200g4100g50.5L60.5L75L80.5kg90.5kg100.5kg110.5kg120.5kg130.5kg140.5kg150.5kg160.5kg170.5kg181910.5kg2020.5kg2130.5kg220.5kg231.0L211.5×2×3121.5×2×3133500r/min14GK-10B25BOD100K16COD100K1750mL100860950mL10104AM-NRV-22F211Minipump2123133.1NO3-3.1.12440。、、、、、、。、pH、、、、。。3.1.2。“”。。A-BNO3-。3.2NO3-30mLNO3-。312.52.5133122.5123132132.5122.5。3NO3-ABNO3-/mg/LNO3-/mg/L1113200020011.51.5320001551223200010012.52.53200030133320000122.5320003512332000101323200028132.532000123.330mL122.520min、25min、30min、35min、40min、45min、50min、55min、60min、70min、80minNO3-2。240minNO3-35mg/L45minNO3-≤15mg/L。3.4NO3-30mL122.545min3。3NO3-0~10℃NO3-≥40mg/L。20~80℃NO3-≤15mg/L《、》NO3-。2NO3-3NO3-3.5pHNO3-pH2.3NaOHH2SO4pH1~10pHNO3-。30mL122.545min25℃4。4pH1~4NO3-≤40mg/L。pHNO3-345。NO3-pH≤4.0。3.6NO3-32000mg/L。NO3-NO3-NO3-NO3-NaNO3NO3-。5。5NO3-5000~50000mg/LNO3-≤15mgL-1《、》NO3-。4pHNO3-5NO3-4⑴A-B⑵NO3-AB122.5⑶40min⑷pH≤4.0⑸20~80℃⑹NO3-5000~50000mg/LNO3-≤15mgL-1《、》NO3-。《》《、》。NO3-。。1AhnJHKwang-HoChooKHParkHS.Reverseos-mosismembranetreatmentofacidicetchantwastewatereffectofneutralizationandpolyelectrolytecoatingonnitrateremovalJ.JMembrSci.2008310296-302.2RivettMOBussSRMorganPetal.Nitrateattenua-tioningroundwaterareviewofbiogeochemicalcontrollingprocessesJ.WaterRes.2008424215-4232.3WangQHFengCPZhaoYZetal.Denitrificationofnitratecontaminatedgroundwaterwithafiber-basedbiofilmreactorJ.BioresourTechnol.20091002223-2227.4PrusseUVorlopKD.Supportedbimetallicpalladiumcatalystsforwater-phasenitratereductionJ.JMolCatalAChem.2001173313-328.5FanXMGuanXHMaJetal.Kineticsandcorrosionproductsofaqueousnitratereductionbyironpowderwithoutre-actionconditionscontrolJ.JEnvironSci.2009211028-1035.6ShinKHChaDK.Microbialreductionofnitrateinthepresenceofnanoscalezero-valentironJ.Chemosphere200872257-262.7WangLSakamotoYKamiyaY.Remediationofactualgroundwaterpollutedwithnitratebythecatalyticreductionovercopper-palladiumsupportedonactivecarbonJ.ApplCatalAGeneral2009361123-129.8.M.1986204.9R.M.196257.2018-05-221978-。2006。、。4440

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