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無機高分子聚合鐵鹽類混凝劑制備方法評述
摘要:綜述了無機高分子聚合鐵鹽類混凝劑的幾種生產制備方法。對用硫酸亞鐵經(jīng)催化氧化法和直接氧化法制備聚合硫酸鐵,用各種含鐵工業(yè)廢渣制備復合聚鐵,以及采用生物和電化學方法制備聚鐵類混凝劑等方法的優(yōu)缺點等作了較全面評述。還對固體聚合鐵的生產及液體聚合鐵混凝劑的穩(wěn)定性進行了討論,對目前聚合鐵生產中存在的問題及發(fā)展方向提出了建議。
關鍵字:聚合硫酸鐵
硫酸亞鐵
混凝劑
硫鐵礦燒渣ProgressonManufacturingMethodofInorganicPolymerCoagulantPolyferricsaltcategoryAbstract:Thispapergivesareviewofthemanufacturingmethodofinorganichighpolymercoagulantpolymerizedferricsulfate.ThepresentsituationofthestudiesandtheproductionofPFSisdiscussed.ItpointsoutthemeritandtheshortcomingofthemanufacturingmethodsofPFSwithferroussulfate,pyritecinderandotherslagscontainingiron.SomesuggestionsaboutpresentproblemsanddevelopmentdirectionintheproductionofPFShavebeenputforward.Keywords
Polyferricsulfate,ferroussulfate,coagulant,pyritecinderIntroduction
Polymerizedferricsulfate(PFS)isanewinorganichighpolymercoagulant.ItsmolecularformulaisFe2(OH)n(SO4)3-n/2]m,(n>2,m=f(n)).Itcanbeusedinwastewatertreatmentandthepurificationofdrinkingwater[1].Comparedwithgeneralinorganiccoagulants,forexample,ferroussulfate,ferricchloride,aluminumchloride,aluminumsulfate,alumflocandpolymerizedaluminumchloride(PAC),PFSisthebestcoagulant.Itscoagulatingabilityisstrong,sinkingspeedisquick,andproducingcostislow.Inaddition,theleavingofaluminumismoreinthewatertreatedwiththecoagulantscontainingaluminum,anditisharmfultothehealthofhumanbody[2].Thisrestrictsthedevelopmentofaluminumcoagulants,andparticularlyindrinkingwatertreatment.Nevertheless,theleavingofferricislittleinthewatertreatedwithPFS,anditisnotharmfultohumanbody.Atthesametime,PFSisalsosuperiortoorganiccoagulantssuchaspolyacrylamide(PAM)insomeindustrialwastewatertreatment[3].WhenPFSsubstitutedforPAMinwatertreatment,theharmofmonomerAM,whichwasleftinwaterafterPAMwasdegraded,couldbeavoided.SotheapplicationprospectofPFSisverygoodandthemarketcompetitionpowerisstrongerinindustrialwastewatertreatment,industrailusingwater,andlifedrinkingwater.
In1972,JapanputforwardPFSasoneofcoagulants,andappliedforthefirstpatent[4]ofPFSmadefromferroussulfate.Thenindustrialscopeproductionandapplicationinwatertreatmentwereformed.ChinastartedthestudiesofPFSin80'searly.ThemanufactureofPFSmadefromferroussulfatewasdevelopedsuccessfullybyTianjinResearchAcademiesofChemicalIndustryunderMinistryofChemicalIndustryofChinain1982.TheproductionofPFSwasindustrialized[5]in1984.Hereafter,popularizingapplicationstepbystepinWuhanironandsteelcompany,etc.Now,PFShasbeenuniversalconcernedandappliedinChinaasanewinorganichighpolymercoagulant[6].Atpresent,themajormanufacturingmethodofPFSistheoxidationmethodofferroussulfate.Ferroussulfateandsulfuricacidareimportantrawmaterialsinthismethod.PFScanbemadebytheoxidationofferroussulfateandthehydrolysisandthepolymerizationofferricsulfate.Anothermethodisthatsomeironoredregs(orwasteresidue)andsulfuricacidareusedastherawmaterialsofPFS.Ironoredregsaredissolvedinsulfuricacid,thenhydrolysis,polymerization.1ManufactureofPFSwithferroussulfate
Ingeneral,ferroussulfate,whichisaby-productproducedintheproductionprocessoftitaniumwhite(titaniumdioxide),andsulfuricacidareusedastherawmaterialsofPFS.Besides,acidwashingwasteliquids,scrap-iron,andsulfuricacidcanalsobeused.Inthemanufacturing
processofPFS,thereactionsofoxidation,hydrolysis,andpolymerizationareallexistentialatthesametime.Becauseofthecauseofdynamics,theoxidizingreactionofferroussulfateisslowerunderaciditycondition.Sotheratecontrollingstepofthereactionsystemistheoxidizingreaction.Thisreactionmaybedirectedoxidationorcatalyzedoxidationaccordingtodifferentoxidizingprocess.1.1Methodofdirectedoxidation
Themethodofdirectedoxidationisthatferroussulfatewasoxidizeddirectlyintoferricsulfatebyoxidizer.Theoxidizerusedherewashydrogenperoxide[7],manganesedioxide,potassiumchlorate[8],sodiumpersulfate,sodiumhypochloriteornitricacidandsoon.Theoxidizingreactioncanbecompletedwithintwohoursundertheconditionofroomtemperaturewhenhydrogenperoxideisusedasoxidizer:
2FeSO4+H2O2+H2SO4=Fe2(SO4)3+2H2O(1)Then,hydrolysisandpolymerization:
Fe2(SO4)3+nH2O=Fe2(OH)n(SO4)3-n/2+n/2H2SO4
(2)
m[Fe2(OH)n(SO4)3-n/2]=[Fe2(OH)n(SO4)3-n/2]m(3)Thetimeoftheoxidizingreactionmaybeshortenedfurtherundertheconditionof50℃.
Themethodofdirectedoxidationhassomemerits,suchassimpleprocess,easyoperation,andshorterreactiontime,buttheconsumptionofoxidizersishighandthepriceisexpensive.SoPFSmadebythemethoddoesnothavemarketcompetitionpower.
Inthemethodofdirectedoxidation,literatures[9]putforwardanotherwaywhichwaseasytooperateandpopularize.Thewaywasbasedonsomefeaturesoftheinstabilityofferroushydroxideandbeingeasytobeoxidizeintoferrichydroxide.Firstly,ferroussulfatewaschangedintoferroushydroxidebyaddingalkaliinthesolutionofferroussulfate:
FeSO4+2NH3·H2O=Fe(OH)2+(NH4)2SO4
(4)Secondly,ferroushydroxideforminginthereactionabovewasoxidizedintoferrichydroxideafterbeingplacedinair:
4Fe(OH)2+O2+2H2O=4Fe(OH)3
(5)Then,oxidizersolutionwasobtainedthoughthereactionbetweenhydrogenperoxideandferroussulfateaccordingtotheequation(1).Finally,PFSwasmadebymixingtheferrichydroxidesuspensionandtheoxidizersolutionwithin2hoursunderthestirredcondition.
2Fe(OH)3+H2SO4+Fe2(SO4)3?[Fe2(OH)n(SO4)3-n/2]m+H2O(6)
Thesereactionsmentionedabovecantakeplaceinroomtemperature.TheprocessingequipmentofthemethodaresimpleanditiseasytooperateandthecostofPFSislowtoo.
Literature[9]reportedthatthestabilityofPFSmadeinthiswaywaspoorer.Infact,theinstabilityofPFSmadeinothermethodsmentionedinfollowingisexistenttoo.ThecriticalfactorsaffectingthestabilityarepH,Fe3+/SO42-oraddingstabilizerinPFS.1.2Methodofcatalyzingoxidation
Themethodofcatalyzingoxidationisthatferroussulfateisoxidizedintoferricsulfatebyoxidizerundertheeffectofcatalyst.ItisamajormethodofmanufacturingPFSwithferroussulfate.Manystudies[10-15]havebeenmadeinthisaspect.Undertheconditionsofhavingoxidativecatalyst
andsuitabletemperature,PFScanbemadethroughtheoxidationofferroussulfate,hydrolysis,andpolymerization.Thecatalystsusedinthereactionofcatalyzingoxidationweresodiumnitrite,manganesedioxideorchloride.Atpresent,themostproductioncompaniesofPFSusethismethod.
ThemanufactureofPFSwithferroussulfateandsulfuricacidwasreportedfirstlybyJapanpatent[4].Whensodiumnitriteandairwereusedascatalystandoxidizerrespectively,themechanismofcatalyzingoxidationcanbeshowedasfollows:
2FeSO4+H2SO4+2NaNO2=2Fe(OH)SO4+Na2SO4+2NO
(7)
FeSO4+NO=Fe(NO)SO4
(8)
2Fe(NO)SO4+1/2O2+H2SO4=Fe2(SO4)3+2NO+H2O(9)
2NO+O2=2NO2(10)
2NO+1/2O2=N2O3
(11)
2FeSO4+N2O3+H2O=2Fe(OH)SO4+2NO(12)or
2FeSO4+N2O3+H2SO4=Fe2(SO4)3+2NO+H2O(13)
2FeSO4+NO2+H2O=2Fe(OH)SO4+NO
(14)or
2FeSO4+NO2+H2SO4=Fe2(SO4)3+NO+H2O(15)
Ferricsaltsproducedinthesereactionswerehydrolyzedandpolymerized:
2mFe(OH)SO4+(1-n/2)mH2SO4=[Fe2(OH)n(SO4)3-n/2]m+(2-n)mH2O
(16)or
Fe2(SO4)3+m×nH2O=[Fe2(OH)n(SO4)3-n/2]m+nm/2H2SO4(17)
ItcanbeseenfromthereactionsabovethatthemechanismoftheoxidizingreactionofferroussulfatehadbeenchangedowingtotheparticipationofNOwhichmadetheoxidizingreactioneasy.Thecatalyzingoxidationtimewasshortenedto4~5hoursfromoriginal17hours.Evenso,thetimewasstilllongerandtheconsumptionquantityofcatalystwasalsomore.Meanwhile,nitrogenoxidesweredischargedintoairinthemanufacturingprocessofPFSandthisresultedintheenvironmentalpollution.
Forthesakeofshorteningthereactiontime,somemeasuressuchasheatingandhighpressureandstrongstirring,wereoftenadoptedinthemanufacturingprocess.Amongthem,themethodoftwostepsoxidationcouldshortenthetime.Firstly,ferroussulfatewasoxidizedintoferricsulfateundertheheatingcondition.Secondly,bothferroussulfateandhydrogenperoxidewereaddedinthesolutionofferricsulfatemadeaboveaccordingtoproportion.Then,PFSwasobtainedafteronehourreactionunderthestirredcondition.
Inordertoavoidpollution,Shortenfurtherreactiontime,andreduceenergyconsumption,themanufacturingtechnologyandthemanufacturingmethodofPFShadbeeninvestigatedthoroughly.Someprogresseshadbeenmade[16],forexample,thecatalysisoxidizingreactiontakenplaceinahermeticcontainerandtheproportionofSO42-/Fe3+wascontrolledinthereactionsystem.Inaddition,takingtheplaceofair,oxygenwasusedasoxidizer.Insuchsituation,PFSwasobtainingundertheconditionofstirringstronglywithin1.5~2hoursand55~90℃and29.4-147′104Pa.Neverthelesstheseconditionsofhightemperatureandhighpressureandstrongstirringwillincreasethedifficultyoftechnologyandtheinvestmentofequipments.Furtherimprovementwasthatthespeedofaddingsulfuricacidwascontrolledandsodiumnitritecatalystwasaddedinbatchesintheoxidizingprocessofferroussulfate.Undertheconditionsofnormalpressureandabove40℃,theoxidizingreactioncouldachievedwithin2-3hourswhenoxygenwasusedasoxidizer[13].Thisreportthoughtthatthemethodofaddingsulfuricacid,thatisthePHofreactionsystemwascontrolledincertainscope,wasthekeyofshorteningthereactiontime.BecausetheoxidizingreactionofferroussulfatewasverydifficultintheconditionoflowerPH,butitcouldtakeplaceeasilywhenthePHwashigherthan2.
Inaddition,literature[17]developedanewmanufacturingtechnologyofPFSwithanatomizationmethod,thatis,undertheconditionsofnormalpressureandheating,theatomizationdripofferroussulfatewascontactedwithnitrogendioxideincirculationstate.Theaimofthisprocesswastoraisethecontactareabetweennitrogendioxideandferroussulfatesolution,quickenreactionvelocity,andshortenproductioncycle.TheprocesspioneeredanewwayfortheproductionofPFS.Ofcourse,thiswillalsoincreasethedifficultyoftechnologyandtheinvestmentofequipment.
Moreover,itwasreportedthatthebestkindofcatalysthadbeenfound[18]alreadyuptonow.Thiscatalystwasnotonlyhigheffectivebutnonpoisonous.Whenitwasusedintheoxidizingreactionofferroussulfate,thereactioncouldbecompletedintwohours.WehopeitcanbeusedintheindustrialproductionofPFSearly.
InthemanufacturingprocessofPFSabove-mentioned,thereactionofferrousandnitrogenoxidesbelongstoareactionbetweenliquidandgas.Inordertoincreasetheircontactareaandquickenthereactionspeed,somemeasures,suchasheating,high-pressure,strongstirring,andspraying,wereoftenused.So,thetechnologyofthemethodiscomplicatedandtheinvestmentcostofequipmentisalsohigher.
Besides,inotherreport,potassiumchlorateorhydrogenperoxidewereusedasasubstituteforairoroxygeninthesystemofsodiumnitrite.Althoughthiscanquickenthespeedofcatalysisoxidizingreaction,itincreasestheproductcost,too.1.3Effectofcatalystpromoteronthereactionofcatalyzedoxidation
BecausetheoxidizingreactionisaratecontrollingstepinthemanufacturingprocessofPFS,shorteningthereactiontimehasalreadybecomeafocalpointconcerned.Sopeoplehadmadethoroughstudies[3,6,18]attheaspectsofoxidizer,catalyst,andcatalystpromoter.Literature[3]hadmadesomedetailedstudiesonthekindandtheadditionofcatalysts,theselectionofcatalystpromoters,thetemperatureandtheacidityofreactionsystem.Thisliteraturethoughtthatsodiumiodideasacatalystpromotercouldquickenthereactionspeed.Atthesametime,italsothoughtthatcontrollingthePHofthereactionsystemwasakeytoquickenthespeedofoxidizingreaction.Itdiscussedhowsodiumiodidequickensthespeedoftheoxidizingreaction,too.
Onthebasisofinspectingtheeffectofcatalystsandoxidizersonthespeedofcatalysisoxidizingreaction,literature[6]reportedthatthetracecatalystpromoterofHG-1,HG-2,orHG-3couldnotablyraisethespeedinthereactionsystemofoxygenandsodiumnitrite.Thismadenotonlytheconsumptionofcatalystdecreasesoneathirdbutthereactiontimesshortentwothirds.Inaword,sodiumnitritewasgenerallyusedasthecatalystintheprocessofcatalysisoxidizingreaction.Itshoudbepointedoutthatsodiumnitriteisacarcinogen,andsomenitricoxideswereletintheprocess.Thisresultsinenvironmentalpollution.Inordertosimplifytechnology,cutdownthecostofproductanddecreasepollution,thedevelopmentdirectionofPFSmadewiththecatalysisoxidizingmethodshouldbestudyingandimprovingfurtherthemanufacturingtechnology,anddevelopingnewcatalystsandcatalystpromoterswhicharehigheffectiveandnonpoisonous.2ManufactureofPFSwithslagorwasteresidue
ItisagoodmethodofturningwasteintousefulproducttomanufacturePFSfromslagorwasteresiduecontainingoxidecompoundofiron.Itcannotonlysolvethethree-wasteproblem,andalsocutdownthecostofPFS,simplifymanufacturingtechnology,havebettereconomicbenefit.2.1ManufactureofPFSwithpyritecinder
PyritecindercanbeasarawmaterialofPFS.ThisisoneofmajormethodspreparingPFSwithslagorwasteresidue.Avastamountofpyritecinderisproducedintheproducingcourseofsulfuricacid.Itsmaincomponentsareferricoxideandferriferrousoxide.Attheaspectofthecomprehensiveutilizationofpyritecinder,thegreaterpartofpyridecinderwasusedasanassistantintheproductionofcement.
Ingeneralsituation,totalironcontentisabout65~65%inpyritecinderandferriccontentis96.5%intotaliron.Afterpyritecinderisdissolvedinsulfuricacid,thefiltratingcandirectlybeusedinthemanufactureofPFS.Thishasdevelopedanotherbetterwayforthecomprehensiveutilizationofpyritecinder.ThemanufacturingmethodofPFSusingpyritecinderiseconomical,anditscostisalsolower.Atpresent,manyprogresseshadbeenmadeinthisaspect[19-22].
ThemanufacturingprocessofPFSusingpyritecindermaybedividedintotwosteps.Thefirststepisthatpyritecinderisdissolvedinsulfuricacid:
Fe3O4+4H2SO4=Fe2(SO4)3+FeSO4+4H2O
(18)
Fe2O3+3H2SO4=Fe2(SO4)3+3H2O(19)Thesecondisoxidation,hydrolysisandpolymerization:
FeSO4+2H2SO4+O2=2Fe2(SO4)3+2H2O(20)
Fe2(SO4)3+nH2O=Fe2(OH)n(SO4)3-n/2+(n-2)H2SO4
(21)
mFe2(OH)n(SO4)3-n/2=[Fe2(OH)n(SO4)3-n/2]m(22)
Inthesecondstep,ferroussulfatemaybeoxidizedwithdifferentmethods.Oneisdirectedoxidation[19].Anotheriscatalysisoxidation[41].Moreover,whenthecontentofferroussulfateisverylowinthefiltrating,theoxidationmaybeleftoutandboththehydrolysisandpolymerizationcantakeplacedirectly[21,22].Inthemanufacturingprocess,itisimportanttoimprovethedissolvingrateofpyritecinderfurtherlyinsulfuricacid.Author'sstudiesindicated[23,24]thatthedissolvingrateisconcernedwithsulfuricacidconcentration,temperature,andtheratiobetweensolidandliquid.Becausethedissolvingcourseofpyritecinderisanexothermicreaction,thedissolvingratemayachieve95%undertheeffectofthereactionheat.Thecontentofferrousonlyoccupies3%ofthetotalironcontentinthefiltrating.PFScanbeobtainedthroughthehydrolyzingandthepolymerizingofferricsulfateundercertaincondition.Oxidizerisnotneededinthemanufacturingprocess.Thishasnotonlyeliminatedthepollutionofnitricoxides,andalsosavedspendingandcutdownfurtherthecostofproduct.
WhenPFSmadebyourselveswasusedinthetreatmentofpapermakingwastewater(CODCr=1000mg/L),theremovalrateofCODCrwasmorethan90%astheadditionofPFSwas150mg/L(thatis,[Fe3+]=150mg/L).Inaddition,theremovalrateofCODCrwasmorethan60%inthetreatmentofsaccharinsodiumslatwastewater(CODCr=15000mg/l)astheadditionofthePFSwas800mg/L.
Inordertoraisethedissolvingratefurtherly,pyritecindermaybepreprocessed.First,
ferricoxideinpyritecinderwasreducedasferrousoxideundertheeffectsofbothhightemperatureandreducer.Pyritecinderwaschangedintoreductiondregs.Second,thereductiondregswasdissolvedinsulfuricacid,obtainingmid-productferroussulfate.Final,PFSwasmadethroughoxidationandhydrolysisandpolymerizationasmentionedin1.2.
Itwassaidthatthismethodcanraisetheutilizationratioofpyritecinder,neverthelesstherewasnotonlyoxidizingreactionbutalsoreducingreactioninthemanufacturingprocessofPFS.Soitwillresultinlongerproducingperiodandhigherconsumption,anditspopularizationandapplicationwillbeverydifficult,too.
2.2ManufactureofPFSwithotherslagscontainingiron
Siderite,magnetiteore,ironmud,naturalironsandandopen-hearthfurnacedust[25-28]arealsotherawmaterialsofPFSbesidespyritecinder.Thecontentsofferriferrousoxideandferricoxidearehighinthem,too.
Literature[26]hadobtainedbetterresultinthemanufactureofPFSusingironmud.Ironmudisthewasteproducedintheproducingprocessofdyemediums.Itsmaincomponentareferriferrousoxideandalittleferricoxide,ferrousoxide,andironbesides.InChina,thetreatmentmethodofironmudisgenerallytostoreuportobury.Thiscauseseasilyenvironmentalpollutionagain,andtheusefulresourceinironmudisalsowasted.ItisagoodwayofwastecomprehensiveutilizationforironmudtobeusedastherawmaterialofPFS.
NaturalironsandisakindofrichmineralresourcesoftheDabieshanMountainsarea.Totalironcontentis59.6%init,andferriccontentis41.1%.ItisagoodrawmaterialofpreparingPFS.Literature[27]reported,usingnaturalironsandandsulfuricacidastherawmaterials,highconcentrationPFS(220g/L)couldbemadethroughpickling,oxidizing,andpolymerizing.Then,theliquidPFSwasconcentratedintosolidbyspray-dryingprocess.
Open-hearthfurnacedustisanotherwasteusedalsotomanufacturePFS.Itisthesmokeanddirtintheopen-hearthfurnacesteelmakingwastegas.Thecontentofferricoxideismorethan90%init.Literature[28]reportedthatthedustcouldbeusedastherawmaterialofPFS:Firstly,thedustwasdissolvedinalkalisolutionforremovingsomeimpurityinit.Thecontentofferricoxidewasmorethan99.5%inthedustpurified.ThenPFScouldbemadethroughaciddissolving,hydrolysisandpolymerization.WhenthePFSwasusedtotreatwashingwastewaterofblastfurnacegas,thetreatedefficiencywasverygood.Moreover,becausethereisnototherharmfulioninthePFS,itisverysuitableforthePFStotreatdrinkingwater.
Inotherreports,wasteresiduecontainingferricoxidewasusedtomanufacturingPFS,too.Undercertaintemperatureandpressure,PFScouldbeobtainedbydissolving,hydrolysis,polymerizationwithoutoxidizer.
Onthewhole,themanufactureofPFSbyslagsorwasteresidueisaneconomicalmethod.Thismethodissimplerthanthecatalysisoxidationmethodmentionedabove.Certainly,therearestillsomeproblemsthatshouldbesolvedfurtherlyinthemanufacturingprocessofPFS.Forexample,thedissolvingrateofslagsshouldberaisedagain,soastoraisetheutilizationrateofrawmaterial.Inaddition,thereisexcessiveacidgenerallyinthesolutionofferricsulfateobtainedbydissolvingslagsinsulfuricacid.Thiswillincreasetheconsumptionquantityofotherassistantsinthecourseofhydrolysisandpolymerization.Iftherearesomeharmfulheavymetalsinslagsandwasteresidue,therewillbesomeheavymetalionsinPFS.Thiswillrestrictitsapplicationindrinkingwatertreatment.3ManufactureofPFSwithothermethods3.1Methodofbiologicoxidation
Usingpyrite,coal,sulfur,andhydrogensulfideasrawmaterials,PFScanbemadewiththemethodofbiologiccatalyzingoxidationundertheinfluenceofiron-sulphurbacteria,suchasthiobacillusferrooxidansandthiobacillusthiooxidans.Literature[29]investigatedsomefactorswhichaffectingthemanufacturingofPFSwithbiologicoxidation.ItreportedthatthesefactorswerepH,theadditionofpyrite,temperature,stirring,andreactiontime.UndertheconditionsofpH2.0~2.3,2.8gpyrite/L,30℃,and300r.p.m.,amid-productwasobtainedin10hoursreaction.ThenPXTcoagulant(thatisPFS)wasmadethroughacidification,concentration,andaging.WhenthePXTwasusedtotreatthehighSSashwaterofpowerplant,itcoulddecreasenotonlySSbutpHandF-.
Intheprocessofbiologicoxidation,boththiobacillusferrooxidansandthiobacillusthiooxidansplayanimportantrole.Theyarethepeculiarmicro-organismswhichcanobtaincarbonresourcesfromCO2inairandliveininorganicenvironment.Theycanoxidizeironandreducesulphurintoferricandsulfuricacid,respectively.
ThepreparationofPFSwithbiologicoxidationisaverygoodway.ThewaydoesnotneedanyotherrawmaterialsbesidespyriteandalittledilutesulfuricacidusedtoadjustthepHofreactionsystem.Itischaracterizedbysimpleproces,savingenergy.Nevertheless,manystudiesshouldbedoneifthemethodofbiologicoxidationisusedinindustrialproductionofPFS.Atpresent,thismethodisstillintheinitialstageofstudyanddevelopment.3.2MethodofelectrolyticoxidationItshouldbepointedoutthattheelectrolyticoxidationofferroussulfateisalsoapreparingmethodsofPFS.First,ferroussulfatewasoxidizedintoferricsulfatewithD.C.electricityinelectrolyticbath.Then,PFSwasobtainedthroughthehydrolysisandthepolymerizationofsulfateferric.However,theelectrolyticoxidationexpendsenormouselectricenergy.Itcannotbespreadedandappliedinindustry.4ManufactureofsolidPFS
Ingeneral,theproductofPFSisliquidstate.Thisproducthasthemeritofbeingeasytouseinwastewatertreatmentprocess,butitsshortcomingisthatthecostoftransportationishigherthansolidstatebecauseofitsvalidcomponentlowerthansolid.SosomestudiesaboutthemanufactureofsolidPFShadbeenmade.
SolidproducthadbeendevelopedthoughconcentratingliquidPFS[9,12,15,27],suchasheatingevaporization,stoving,andvacuumevaporationanddrying.Wecallthesemethodsthetwo-stepprocessasitincludesboththepreparationofliquidPFSandtheconcentration.KreplkaJ[30,31]reportedthatsolidPFScouldbemanufacturedbyoxidizingthesolutionofferroussulfatewithairundertheconditionsof120~180℃and0.3~2.5MPa.Inaddition,PrasakTP[32]developedasimplemethodofmanufacturingsolidPFS:firstly,preparingsolidbasicferricsulfatebyoxidatingferroussulfatewithairinarevolvingblastfurnaceundertheconditionsof200℃and3hours,andthenobtainingsolidPFSbymakingthesolidbasicferricsulfatereactswithsulfuricacid.Theshortcomingofthemethodisthattheoxidationofferroussulfateisnotcompleteinthefirststep.Usingsolidrawmaterials,LiKechang[33]alsosucceededinmanufacturingsolidPFSthroughsolidphasereaction.
Recently,WangDuoren[34]reportedthatsolidPFScouldalsobemadebyone-stepprocess.First,mixturingthesolutionofpotassiumchlorateandthesuspensionofferroussulfate.Then,obtainingsolidgranulatedPFSundertheconditionsof100℃andpH2-3after1hourreaction.
AlthoughhavingovercometheshortcomingofthehightransportationcostofliquidPFS,solidPFSconsumesenormousheatenergyinmanufactureprocess,andithavetobedissolvedagainbeforebeingusedinflocculationprocess.SothesuitablemethodofmanufacturingPFSshouldbetomakehighconcentrationliquidPFS.
5StabilityofPFS
IfliquidPFSislong-termstored,Fe(OH)SO4sedimentwillbeproducedinPFSsolution,thatis,liquidPFSisunstable.ThestabilityofPFSisaveryuniversalandveryimportantproblem,anditmustbeconsideredinthemanufactureandtheapplicationofPFS,butthisproblemisreportedseldominmostliteraturesaboutPFS.
LiuChangrangetal.[9]hadstudiedthestabilityofPFSandpointedoutthatliquidPFS,whichwasmadefromferroussulfatewithcatalysisoxidationmethod,wasunstable.OnestabilizerwasaddedinliquidPFSinordertostrengthenthestabilityofPFS.Inaddition,ShuWangenetal.[35]andWangShicaietal.[36]hadstudiedthestabilityofpolymerizedferricchlorideandpolymerizedaluminumsulfate,respectively.TheirexperimentalresultsshownthatstablepolymerizedferricchloridecouldbemadebyaddingstabilizerS-3insolution,andtartaricacidwasagoodstabilizerofpolymerizedaluminumsulfate.
Author'sstudiesindicatethatliquidPFSmadewithothermethodsalsohastheinstability.ThestabilityofPFSisrelatedtothePHofsolutionandtheconcentrationofSO42-insolution.So,besidesaddingsomestabilizersinPFS,bothadjustingthepHandcontrollingtheconcentrationofSO42-areaeffectivemethod,too.
Finally,itshouldbepointedoutthatchangingliquidPFSintosolidthroughevaporationanddryingisagoodwayofsolvingtheinstabilityofliquidPFS.6Conclusion
Comparingwithothercoagulants,PFSisthebestkindofinorganicwatertreatmentagentsanddoesn’tproducetwicepollution.Ithasawideapplicationprospect.Thecatalysisoxidizingmethodofferroussulfatehadbeenpopularizedandappliedinindustrialproduction.ItisamajormanufacturingmethodofPFSatpresent.However,therearestillsomeproblemswhichshouldbesolvedinmanufacturingprocess.
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