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OpenJournalofNatureScience,2019,7(5),382-386PublishedOnlineSeptember2019inHans.://doi.org/10.12677/ojns.2019.75047:.[J].,2019,7(5):382-386.DOI:10.12677/ojns.2019.75047StudyonTreatmentofHighAmmoniaNitrogenWastewaterbyAdvancedOxidationProcessinAmmoniaSynthesisProcessHongbinZhangSyntheticAmmoniaPlantofDaqingPetrochemicalCompanyofChinaPetroleumCorporation,DaqingHeilongjiangReceived:August5th,2019;accepted:August20th,2019;published:August27th,2019AbstractInthispaper,highammonianitrogenwastewaterwasusedastheresearchobjectintheammoniaprocess.Theadvancedoxidationmethodwasusedasthetreatmentprocesstostudythedegrada-tionreactioncharacteristics.Themainoperatingconditionsoftheprocess,suchasreactionpres-sure,reactiontemperature,reactionresidencetimeandoxidantdosage,wereinvestigated.Theeffectofwastewatertreatmentandwetoxidationhasgoodtreatmenteffectundersufficientoxi-dantadditionconditions,andthebestreactionconditionsareobtained:reactiontemperature305?C,pressure14MPa,oxidantdosage200mg/L,residencetimewas9min,andtheCODremovalratewas81.6%.KeywordsWetOxidation,AmmoniaNitrogenWastewater,COD,Oxidant20198520198202019827DOI:10.12677/ojns.2019.7504738330514MPa200mg/L9minCOD81.6%CODCopyright?2019byauthorandHansPublishersInc.ThisworkislicensedundertheCreativeCommonsAttributionInternationalLicense(CCBY).[1][2][3][4](BNR)[5]BNR[6](150~3505~20MPa)[7][8][9][10]2.COD5001000150020002500mg/L25min225~3056~14MPa35%333.3.1.COD14MPa305200mg/LOpenAccessDOI:10.12677/ojns.2019.75047384COD1Figure1.EffectofreactionresidencetimeonCODremovalrate1.COD1COD3059minCOD81.6%3.2.COD14MPa200mg/L9minCOD2Figure2.EffectofreactiontemperatureonCODremovalrate2.COD2COD225~245CODCODDOI:10.12677/ojns.2019.75047385285COD3.3.COD3059min200mg/LCOD3Figure3.EffectofreactionpressureonCODremovalrate3.COD3COD6MPaCOD58.8%10MPaCOD75.9%14MPaCOD81.6%3.4.COD30514MPa050100150200mg/LCOD4Figure4.EffectofoxidantdosageonCODremovalrate4.CODDOI:10.12677/ojns.2019.750473864CODCOD58.6%100mg/LCOD75.2%200mg/LCOD81.6%23%(2O-?HO2?)4.CODCOD30514MPa9min200mg/L[1]Bao,Y.F.,Li,M.andZhang,Q.(2016)ResearchontheLarge-ScaleApplicationofNitrogenRemovalfortheTreat-mentofSyntheticAmmoniaWastewater.DesalinationandWaterTreatment,57,12763-12769.[2]Guo,C.H.,Stabnikov,V.andIvanov,V.(2010)TheRemovalofNitrogenandPhosphorusfromRejectWaterofMu-nicipalWastewaterTreatmentPlantUsingFerricandNitrateBioreductions.BioresourceTechnology,101,3992-3999.[3]Liu,J.Y.,Luo,J.H.,Zhou,J.Z.,Liu,Q.,Qian,G.R.andXu,Z.P.(2012)InhibitoryEffectofHigh-StrengthAmmoniaNitrogenonBio-TreatmentofLandfillLeachateUsingEGSBReactorunderMesophilicandAtmosphericConditions.BioresourceTechnology,113,239-243.[4]Zhang,T.,Ding,L.L.,Ren,H.Q.andXiong,X.(2009)AmmoniumNitrogenRemovalfromCokingWastewaterbyChemicalPrecipitationRecycleTechnology.WaterResearch,43,5209-5215.[5]Sui,Q.,Liu,C.,Zhang,J.,Dong,H.,Zhu,Z.andWang,Y.(2016)ResponseofNitriteAccumulationandMicrobialCommunitytoFreeAmmoniaandDissolvedOxygenTreatmentofHighAmmoniumWastewater.AppliedMicrobiol-ogyandBiotechnology,100,4177-4187.[6]Joo,H.S.,Hirai,M.andShoda,M.(2005)NitrificationandDenitrificationinHigh-StrengthAmmoniumbyAlcali-genesfaecalis.BiotechnologyLetters,27,773-778.[7],.4-[J].,2008,21(1):192-195.[8],.-[J].,2012(10):176-181.[9],,.Fe/[J].,2002,39(3):42-44.[10],,,.Fe/[J].,2016(1):33-36.1.://scholar.cnki.net/new[ISSN]ISSN2330-17242.://://@hanspub.org