同济大学环境工程学院(上海,200092) 李风亭 ,,。 ,,,,,,。,。Fe3(OH)45+、Fe4O(OH)46+、Fe6(OH)126+,,、、,COD、BOD、、、,pH。、、、、。,,,,,1t,,,,。,〔1〕。1 ,。、、、,,,。H2SO4,。,。〔2〕。:H2SO4+2MNO22HNO2+M2SO4(1)H2SO4+2HNO2+2FeSO4Fe2(SO4)3+2NO↑+2H2O(2)2NO+O22NO2↑(3)H2SO4+NO2+2FeSO4Fe2(SO4)3+NO↑+H2O(4):4FeSO4·7H2O+(2-n)H2SO4+O2 2Fe2(OH)n(SO4)3-n/2+(30-2n)H2O(5) ,M,0≤n2。,,NONO2,NO,NO2。,,。,。,,。2 ,5 .,1992,12(6):22~246 ,.,1993,13(4):7~117 .,1989,9(5):14~168 .’96,1996.19~239 WangZumo,ChenKang.IWC-91-6,1991.56~6110 .’97,1997.57~59:,1970,1994,,,。收稿日期:1998-03-03—9—工业水处理1998—09,18(5) 国外氮氧化物催化法合成聚合铁新工艺,,1〔3〕。图1 利用静态混合器生产聚合硫酸铁工艺流程1. 2. 3. 4. 5. 13,,,、,1,。,,。 〔4〕。,,,,。,,。 Derka,〔5〕。70℃~150℃,,,。,。,,,,。 ,,,。,,,,。:、、、。,,,、,,30~40min1t。 。,、,,,,,,。—。,,。,。,,。 ,,,,。,,,,。1 ,,.,1995,11(1):422 .,1994,10(8):393 JP950580384 JP950547045 US5194241:,1963,1997,,,。收稿日期:1998-03-16—10—试验研究 工业水处理1998—09,18(5)DEVELOPMENTANDAPPLICATIONOFMODIFIEDCATIONICNATURALPOLYMERFLOCCULANT YinHua,PengHui,XiaoJin(Dept.ofBiologicalEngineering,Ji-nanUniversity,Guangzhou510632):Chin.J.Ind.WaterTreat.,18(5),1998,pp.1~3 Themodifiednaturalpolymerflocculantpossessesmanyadvantages,thusgreatattentionhasbeenpaidtoitsdevelopmentandapplicationbyscholarsbothathomeandabroadinrecentyears.Inthispaper,theprogressofre-searchandapplicationofthederivativesofmodifiedcationicstarch,lignin,chitinwhichhavebeenusedinwastewatertreatmentandplantgumwhichhassomeotherfunctionsinadditiontoflocculationhasbeenbrieflyreviewed. Keywords starch,lignin,chitin,cationicflocculantDISCUSSIONSONTHESUSTANABLEDEVELOPMENTOFWATERANDWASTEWATERINDUSTRY QiLianhui(Bei-jingCentralEngineeringandResearchIncorporationofIronandSteelIndustryCERIS,Beijing100053):Chin.J.Ind.WaterTreat.,18(5),1998,pp.4~6 Sustanabledevelopmentofthewaterandwastewaterindustryisdiscussedtheoreticallyandrealistically.Thedi-rectionandmanagingstepsaregiven. Keywords waterandwastewaterindustry,sustan-abledevelopment,managingstepsSTUDYOFTHESYNTHESISANDPERFORMANCEOFPHOSPHORUS—CONTAININGPOLYMERS YangWen-zhongLuChangqing,WangYongetal.(NanjingChemicalIndustryUniversity,Nanjing210009):Chin.J.Ind.WaterTreat.,18(5),1998,pp.7~8 Thesynthesisofisopropylenephosphoricacid(IPPA)andco-polymerizationofIPPAwithacrylicacid(AA)、2-acrylamide-2-methylpropanesulfonicacid(AMPS)topreparecopolymerAA/IPPA/AMPSweredescribed.Thescale-corrosioninhibitionofAA/IPPA/AMPSandotherpolymerswereevaluatedandcompared. Keywords polymer,scale-corrosioninhibition,per-formanceevaluationNEWPROCESSABROADFORTHEPREPARATIONOFPOLYFERRICSULFATECATALYZEDBYNITRICOXIDE LiFengting(SchoolofEnvironmentalEngineering,TongjiUniversity,Shanghai200092):Chin.J.Ind.WaterTreat.,18(5),1998,pp.9~10 Thepaperreviewsafewofnewprocessesabroadforthepreparationofpolyferricsulfateandpolyferricchlo-ride,whicharecatalyzedbynitricoxideintheabsenceofoxygenorair.Therearemanyfactorsaffectingthereactiontime.Accordingtopreviousexperience,weappraisethetechnologicalfeaturesandbringupsomemeasurestoen-hanceproductionefficiency. Keywords polyferricsulfate,polyferricchloride,preparation,catalysis,nitricoxideTHERESEARCHANDPREPARATIONOFASLOW-DIS-SOLVEDPHOSPHATEWATERTREATMENTAGENTANDITSUSESINBOILERWATERTREATMENT LiuZhenfa,WangYulin,JiBaoxia(TheInstituteofEnergySources,HebeiAcademyofSciences,Shijiazhuang050081):Chin.J.Ind.WaterTreat.,18(5),1998,pp.11~12 Thesynthesisofaslow-dissolvedphosphatewatertreatmentagentisintroduced.Itsperformanceofscaleinhi-bitionandanti-corrosionisstudied.Theapplicationofthiswatertreatmentagenttolow-pressureboilerwatertreat-mentshowsthatthiswatertreatmentagentisconvenientinoperation,lowinwatertreatmentcostandveryefficientinscaleinhibitionandanti-corrosion. Keywords phosphate,watertreatment,scaleinhibi-tion,anti-corrosionRESEARCHESONTHEDECOLORIZATIONOFHIGHCOL-ORITYDYEINGWASTEWATER LiuYi,ZhangJianhui,LiangLongwuetal(DepartmentofChemistry,ZhongshanUniversity,Guangzhou510275):Chin.J.Ind.WaterTreat.,18(5),1998,pp.15~16 Anewmethodhasbeenestablishedfordecoloringofhighcoloritydyeingwastewaterwithoxide-flocculationre-actor(OFR)technique.Themechanismofdyeandothercontaminantsremovalisactuallytheoxidationofhydroxylradical(·OH).Variousfactorswhetherphysicalorchemi-cal:cellvoltage,mainelectrodedistance,testingsolution,pHvalue,airflowrate,treatingtimeetc,whichaffectedthedecoloringratehavebeenstudied.Theresultsofcon-taminantsremovalindyeingwastewaterforcolority10000undertheopticaltestingconditionwereverygood:de-coloringrate99%,CODCrremovalrate75%. Keywords dyeingwastewater,decolorization,oxide-flocculationreactorEXPERIMENTALSTUDYONTHETREATMENTOFACID-BEARINGWASTEWATERFROMSULPHAMIDEPRODUC-TION GaoJun,DiaoLitong,LiXinjun(DepartmentofChemicalEngineering,InnerMongoliaPolytechnicUniver-sity,Huhhot010062):Chin.J.Ind.WaterTreat.,18(5),1998,pp.17~18 Treatmentonacid-bearingwastewaterfromsul-phamidemanufacturingwasstudied,takingcalciumcarbidedregsasneutralizerinthispaper.Theinfluencesonpro-cesseswereexamined,andthetechnologicalconditionsweredetermined.Theexperimentalresultsshowedthattreatedwastewa