奥托昆普哈加瓦尔塔镍加压浸出流程1.docx
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奥托昆普哈加瓦尔塔镍加压浸出流程1.docx
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奥托昆普哈加瓦尔塔镍加压浸出流程1
NEWNICKELPROCESSINCREASINGPRODUCTIONATOUTOKUMPUHARJAVALTAMETALSOY,FINLAND
TABLEOFCONTENTS
1.0Introduction2
2.0NickelSmelter3
3.0Nicke!
Refinery5
4.0Conclusions18
Presentedat
ALTA1997Nickel/CobaltPressureLeaching&Hydrometallurgy
Forum,May19-20,1997,PerthAusffalia
1.0INTRODUCTION
OutokumpuOyhasproducednickelatHarjavaltaWorksinFinlandsince1960.Theproductionhasbeenbasedonflashsmeltingtechnologyandelectrowinningofnickel.Thecapacityoftheprocesshasbeenincreasedgraduallyto18000tpabyseveralsmallexpansionsandprocessimprovements.TheproductionreliedondomesticnickelconcentratesuntilthaAttheturnofthe1990sanewnickelstrategywasdevelopedandOutokumpustartednickelexplorationinAustraiiaandCanada.TheworksecuredlongtermdeliverycontractsofnickelconcentratesfromMt.KeithandstartingofminingoperationsatForrestaniaandSilverSwaninAustralia.
AtthesametimeOutokumpustudieddifferentalterativestoexpandthenickelandcopperproduction.n1993,adecisionwasmadetoinvestintheexpansionandmodernisationofHarjavaltaoperations.Outokumpudecidedtoincreasenickelproductionfrom18000tpato32000tpaandblistercopperproductionfrom100000tpato160000tpa.ThecopperrefineryinPoriwasexpandedfrom72000tpato125000tpa.Inaddition,theexpansionincludedanewoxygenplant,twohydrogenplantsandanewsulphuricacidplant.Theconstructionstartadin1993andtheHarjavaltaprojectwascompletedin1996.Duringtheconstructionthenickelproductionwasdecidedtoincreasefurtherto40000tpa.TherealisedcapitalexpenditureofthewholeexpansionprojectofHarjavaltawasFIM1600million($US370million).
Theexpansionofthenickelproductionhasmeantseveralprocesschangesinthanickelsmelterandrefinery.ThedecisiontoinvestinnickelwasprecededbyresearchanddevelopmentworkatOutokumpuHarjavaltaMatalsOyandatOutokumpuRasaarchOy.Theinvestigationprogramledtothefollowingimprovementsoftheprocess:
DevelopmentofdirectOutokumpuNickelSmelting(DON)Process.
Leachingprocessforhighironnickelmatte
UtilizationofOutokumpu-developedanddesignedreactorsforatmosphericandpressureleaching.
UtilizationofOutokumpu-developedsolventextractionprocessinthenickel/cobaltseparation
UtilizationoftheSherrittprocessforhydrogenreductionofnickalandcobalt.
Sulphuroutletasammoniumsulphate
Theprocessimprovementswereincorporatedintheexistingnickelflashsmelter,matterefineryandelectrowinningprocaiss.Thecapacityofthenickelrefineryis18000tpanickelcathodesand22000tpabriquettes.
2.0NICKELSMELTER
Intha1980sOutokumpustartedtodevelopaconverterlessdirectsmeltingprocesstopraduceahighgradenickelmatteforfurtherrefining.TheprocesswastestedonapilotscaleatOutokumpuResearchOyinPoriandfoundtobeviable.ThebenefitsofthisprocesswereinasimplifiedflowsheetandhighgradeS02gasflowtotheacidplant.TheprocesswasnamedthedirectOutokumpuNickelSmeltingProcessorDONProcess/1-3/.
Attumof1990sOutokumpucontinuedthedevelopmentworkontheDONProcessbasedonafeedwithhighnickelandmagnesiacontentandlowironcontent.AsaresultofthisworktheDONPrccesswasfurtherdevelopedtoproducetwomattes:
Lowironmatteintheflashsmaltingfumace(FSF)tobeleachadintheexistingleachingcircuitofHarjavalta.
Highironmatteintheelectricfurnace(EF)tobeIeachedinanewEFmatteleachingcircuit.
Byproducingtwomattesitwaspossibletoeliminatetheconverterswhichhasmeantasimpleprocesswithlowinvestment,maintenanceandoperatingcosts.Inaddition,itisnowpossiblatosmeltconcentrateswithahighmagnesiumcontent.TheferricresiduefromtheEFmatteleachingisaddedtothesmeltingchargetoincreasetheirontomagnesiumratioandtoreducesmeltingtemperatureoftheslag.Futher,thecobaltrecoveryoftheDONPracessishigherthanintheconventionalsmeltingprocess.
InHarjavalta'scase,itwasessentialthattheprocesscouldusetheexistingflashfurnaceandelectricfurnaceaswellastheexistingleachingplant.FigurelshowstheflowsheetoftheDONProcessatHarjavaltanickelsmelter.
Theprimaryfeedofthenickelsmelterisablendofvariousconcentrates.Alsonickelcontainingsecondarymaterialsareusedasafeed.Inadditiontothefluedustfromthewasteheatboilerandtheelectrostaticprecipitator,theironprecipitatefromtheEFmatteleachingiscirculatedbacktotheflashfurnace.Thismakesitpossibletoconvertleachresiduetodisposablefayaliteslag.Concentratesandsandaredriedinanoil-firedrotarydrum.Afterdrying,thefeedmixtureandoxygenenrichedairarefedthroughtheconcentrate'burnerintothereactionshartoftheflashsmeltingfumace.Duringtheoxidationprccesstheironcontentofthenickelmatteiscurrentlyreducedtofivepercent.Thenickeimatteisgranulateddirectlyintowaterdewateredandfedtotheleachingplant.
Theslagfromtheflashfumaceistappedintotheelectricfumaceforcleaning.Inthepurificattonprocess,coalisusedasareductantanddrynickelconcentrateasasulphidizingagenttoproduceadesiredqualityofmatteandslag.ThematteisgranulatedbyasimilarprocassasusedfortheFSFmatteandisfedtothenewEFmatteleachingplant.TheslagfromtheEFfumaceisalsogranulatedandfinailystoredinslagdumps.
Hotgasfromtheflashfurnaceiscooleddownto350℃inawasteheatboilerandbeforefeedingtotheacidplant,dustisremovedinanelectrostaticprecipitator.
Tablelgivesatypicalcompositionofthefeedmixture,flashfurnacematte,andelectricfurnacematteandslags/4/.
Thesmeltingcapacityofconcentratesis250000tpacorresponding40000tpaofnickelatthecurrentblendofconcentrates.
TablelCompositionoffeedmixture,flashsmeltingfurnacematte,electricfurnacematteandslags.
3.0NICKELREFINERY
AnoyerallflowsheetofthenickelproductionprocessatHarjavaltaisshowninFigure2.ThegranulatedmattesfromtheFSFandtheEFarethestartingmaterialsforthenickelrefinery,where,aftergnnding,themattesareleachedinseparatecircuits.Theproductsolutionfromtheleachingplantisledtoasolventextraction(SX)processforcobaltseparation.TheSXplanthasreplacedtheformercobaltremovalprocess/5,6/,wherecobaltwasprecipitatedasacobaltichydroxide.Therearetwofinalproducts;cathodenickelproducedinanelectrowinningstepandnickelbriquettesproducedinahydrogenreductionstep.Therearealsofacilitiesforhydrogenreductionofcobalt.
Thenickelrefinery,orinfacttheentireHarjavaltaplant,isautomatedusingtheVALMETDamaticXDprocesscontrolsystem.Inthenickelrefinery,OutokumpuMintecon-streamanalysersformanessentialpartoftheautomation,TheCourier30APanalysersmeasureliquidphaseconcentrationsofcopper,ironandarsenicusingX-rayfluorescencewhereasautomaticOTItitratorsareusedformeasuringsulphuricacidconcentration.
3.1LEACHINGPLANT
TheleachingplantatHarjavaltaisespeciallydesignedfortreatmentofthetwomattesfromtheDONProcess.ThechemistryoftheIeachingprocessisdescribedpreinsection3.1.1,whereastheactualcircuitatHarjavaltaanditsparametersaresentedinsection3.1.2.
3.1.1Outokumpunickelmatteleachingprocess
BasedonexperiencesfromtheHajavaltaleachingplantandresearchworkusingsmall-scaleequipment,OutokumpuhasdevelopeditsmethodforIeachingtwodifferentnickelmattes.AflowsheetoftheOutokumpunickelmatteIeachingprocessisshowninFigure3.
AccordingtotheOutokumpunickelmatteleachingconcept,theFSFmatteisleachedinthreestepsconnectedincounter-currentandtheEFmatteisIeachedintwostepsinseries.Mainleachingagentsareoxygenandsulphuricacid.
ThemainproductoftheIeachingplant,i.e.thesolutiongoingtocobaltandnickelseparation,isachievedfromthecopperremovalstep.ThecopperisobtainedascoppersulphideprecipitatefromthenickelIeachingautoclaveintheFSFpressureleachingstep.AnypreciousmetalsintheFSFmattearecollectedintotheresiduefromthetotalIeachingautoclave/7/.TheironisprecipitatedasgoethiteorhematiteintheEFIeachingcircuit.
a)Atmosphericcopperremoval
TheatmosphericcopperremovalintheFSFIeachingcircuitproducesaNi-andCo-sulphatesolutionwithimpuritiesatlevelslowenoughforsubsequentcobaltextractionandnickelreduction.ThemainmineralsinthematteareheazlewooditeNi3S2,coppersulphideCu2SandaNiCualloy.Theotherelementsoccurpartlyinseparatephasesbutalsomixedintothethreemainphases.ThemostreactivephaseisthemetallicalloyfollowedbyNi3S2andthenCu2S.
Importantreactionsaretheprecipitationofcopperandthesimultaneousleachingofnickel.Mostimportantnetreactionsareshowninthefollowing:
CuSO4+NiCu+0.5O2—Cu2O+NiSO4
(1)
2CuSO4+2Ni3S2+0.5O2—Cu2O+2NiSO4+4NiS
(2)
3CuSO4+2Ni3S2+O2+2H2O—Cu3SO4(OH)4+2NiSO4+4NiS(3)
2CuSO4+NiCu+O2+2H2O—Cu3SO4(OH)4+NiSO4(4)
lroninthesolutionsfedtothecopperremovalstepisvirtuallyasFe++,anditisoxidizedandprecipitatedasFeOOHaccordingto
FeSO4+Ni3S2+0.75O2+0.5H2O—FeOOH+NiSO4+2NiS(5)
butsomeFe(OH)3isalsoformed.
Arsenic,antimonyandbismutharemainlyprecipitatedtogetherwithironinpoorlysolubleferriccompoundssimilartoferricarsenate,FeAs04.Thus,theremovaloftheseelementsfromthesolutionisenhancedbyanincreasedironprecipitation.
b)Nickelatmosphericleach
Intheat
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