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    Bioleachingofachalcopyriticoreincolumns

    Fernando

    Torres,

    Adriana

    Tua,

    Miguel

    Mas

    and

    Olga

    Regalado

    UniversidadNacionaldeCatamarca,Argentina

    BlancaEscobar

    UniversidaddeChile

    ABSTRACT

    Bioleachingoflowgradecopperoresisahydrometallurgicalalternativeofgreatimportanceforthe

    future. Many factfinding efforts have focused on recovering sulphur ores from copper. Bio

    hydrometallurgyhasbeenappliedintherecoveryofsecondarysulphidecopperoreslikechalcocite

    andhasobtainedgoodresultsnotonlyinrecoverybutalsoinkineticsbyapplyingbacteriaknown

    as Acidithiobacillusferrooxidans and Acidithiobacillus

    thiooxidans. This research introduces a

    bioleachingtestinaPVCcolumnof1minheightand0.105mindiameter,loadedwith13.31kgof

    copper ore with a grade of 0.41 % of total copper. The applied mineralogy comprises copper

    sulphides, chalcopyriteand covellite, copperoxides (principallymalachite)and abundantpyrite,

    hematiteandmagnetitecontainingimportantquantitiesoffinelimonite.ThemineralsizegaveaP80

    of5,500microns(70% #4,Tyler).Thismineralyieldedlowrecoveriesfromtheflotation,between

    40%and50%.The testwascarriedout in two stages.The first stagewas the leachingprocess,

    whichtookplaceduringfourdaysusingconcentratedsulphuricacidtoextractsolublecopper.The

    secondstageaimedatrecyclingtheacidicsolutionandapplyingabasalculturemediumforan86

    day period of time. Additionally, isolation tests with PLS samples were carried out for At.

    ferrooxidansandAt.thiooxidans,soastodemonstratetheirpresenceasawild type in thismineral.

    Theobtained results suggest thepresenceofbothbacteria,At.ferrooxidansandAt.

    thiooxidans,as

    wellasacloseextractionofcopperof65%for86daysofleaching.Nearly10%ofthisresultcanbe

    assignedtobacterialaction.

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    INTRODUCTION

    Worldwide copper production is continuously increasing. More than 20 % of the manufactured

    copper

    is

    now

    being

    treated

    hydrometallurgically.

    An

    indirect

    indicator

    of

    the

    outstanding

    growth

    in thehydrometallurgicalcopperproduction is the increase in thecapabilityofsolventextraction

    plants (SXEW) to produce copper cathodes. It increased from 0.8 million tonnes to two million

    tonnes between 1993 and 1997 [1]. As the demand of copper grows, the mining industry is

    accessing lowgrade minerals and the methods of treatment must have lower operation and

    inversioncosts.Millionsoftonnesoflowgradeoresonwastedepositsandtailingsarewaitingfor

    the development of an economical and efficient technology to obtain copper of chalcopyrite

    (CuFeS2).Bioleachingoflowgradesulphidemetallicoresisthemostimportanthydrometallurgical

    road and has a promissory future. Since it is an alternative, many factfinding works and

    researchers efforts are intended to enlarge knowledge on this topic. With regards to copper

    extraction, biohydrometallurgy has been applied on secondarysulphide ores of copper as

    chalcocite(Cu2S)withgoodresultsnotonlyinrecoveriesbutalsoinkinetics,particularlyapplying

    bacteria likeAcidithiobacillusferrooxidansandAcidithiobacillus

    thiooxidans,both from themesophile

    group. These bacteria do not behave in the same way when copper ore is in the form of

    chalcopyrite,presentingaveryslowkinetics.

    For these ores, studies are being carried out using bacteria from the group of the moderate

    termophilessuchasAcidithiobacilluscaldusandSulfobacillus thermosulfidooxidans, from theextreme

    thermophilesarchaeasor fromaconsortiaofmoderateandextrememesophilesand termophiles

    suchasSulfolobusmetallicus[3,4],AcidianusBrierleyorMetallospherasedula[2].

    Bioleachingof lowgradecopperminerals isbeingappliedatpresent.Copperprimaryrefractory

    ores like chalcopyrite is less extended. However, applications in waste deposits of lowgrade

    copperarefoundmainlyinChile[1,5].Bacteriaarerecognisedduringthebioleachingprocessby

    their

    catalytic

    action

    in

    the

    natural

    processes

    of

    metal

    separation,

    such

    as

    copper,

    zinc,

    gold

    and

    uranium.Sincethefirstbacteriumwasisolated,manybacteriahavebeenidentified.Inthisprocess,

    Acidithiobacillus stand out and have been largely studied and analysed. Since Acidithiobacillus

    ferrooxidanswasisolated,itwasthoughtthattheonlyimportantmicroorganisminbioleachingcame

    from minerals. Nonetheless, in the last 30 years, many strains have been discovered.

    Acidithiobacillus ferrooxidans is, by now, the more frequently isolated microorganism in the

    bioleachingprocesses.

    Mechanismsofinteractionmineralbacteria

    Bacteria cover its demand of carbon with CO2 as their energetic needs are obtained from the

    oxidationof the ferrous ionaswellas from reducedspeciesofsulphur. In thisway,bioleaching

    occursin

    an

    acidic

    medium

    with

    ferric

    ion.

    Therearetwomechanismsofbacteriainteractionwithsulphideminerals:anindirectmechanism,in

    which the bacteria oxidise iron (II) to iron (III) and the sulphide to sulphate, and a direct

    mechanism that implies thebacteria adhere directly on the solid crystals. In this case, it is a

    sulphideoressentialsulphuractingasbridgetotransferelectrons.

    Lowgrade copper ores and those with low recoveriesbefore flotation due to the presence of

    primarymineralsofcopper,likechalcopyrite,havegonethroughbacterialleaching.Thisisanother

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    possibilityof lowcostextractionthatallowsrecovery;copperwastedeposits,forexample,canbe

    processedbythismethod.

    METHODOLOGY

    Mineral

    The mineral sample was named MM1. The total weight of the lot was 147 kg. To prepare the

    mineralsample,itwasputthroughjawsgrinderat1setopening.Arepresentativemineralsample

    of13.31kgwasextractedandchargedina1mhighcolumnwithadiameterof105mm.

    Chemicalcompound

    The sample for chemical analysis was prepared according to Richards table. The chemical

    compositionofthemineralwas:TotalCu:0.42%;solubleCu:0.13%andtotalFe:5.1%.

    Mineralogy

    The test was performed using a lowgrade copper ore, containing 0.42 % copper, mostly

    chalcopyrite,0.95%,covellite,0.08%,malachite,0.15%,pyrite6.04%,jarosite2.74%bymass,and

    somemagnetiteandhematite.Thisoreshowslowrecoveriesinflotationprocessbetween4050%.

    Somemineralogicalassociationswiththismineralare:

    CovellitereplacingchalcopyriteinthebordersChalcopyriteintergrowthinhematiteHematitereplacingmagnetitePyritereplacedbylimonites.

    Sizinganalysisofthesample

    ParticlesizedistributionsweremadewithamechanicalRoTapsieve,withacapabilityforseven

    sieves.Forthisprocess,Tylersieveswereused.Fortheweight,a2353Sartoriusscalewasused.It

    hasamaximumcapacityof3kgandaccuracy0.1g.Inthefollowingtable,thegrainsizeanalysisof

    thesampleisshown:

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    Table1 Sizinganalysisofmineralsample

    Mesh Fractionsize

    (microns)

    Oversizeweight

    (g)

    Ov.weight

    (%)

    Ov.weightacum.

    (%)

    Passing

    (%)

    4

    4750

    3860

    29.00

    29.00

    71.00

    6 3350 2220 16.68 45.68 54.32

    8 2360 510 3.83 49.51 50.49

    10 1700 760 5.71 55.22 44.78

    14 1180 1140 8.56 63.79 36.21

    20 850 1080 8.11 71.90 28.10

    2830 600 1060 7.96 79.86 20.14

    6570 212 1620 12.17 92.04 7.96

    100 150 620 4.66 96.69 3.31

    100

    440

    3.31

    100.00

    0.00

    TOTAL 13310 100.00

    TESTOFBIOLEACHINGINCOLUMN

    AtransparentPVCcolumnof0.105mofdiameterand1mhighwasfilledwith13.31kgofmineral,

    and watered during 86 days with a solution containing culture medium T&K [7], and pH= 2

    regulated with sulphuric acid, with an irrigation rate of 82 cm3/h and an equivalent flow of 11

    L/h/m2.Thecolumnhadasystem forcollectingsolutionsenablingcleansolutions in itswayout.

    Watering was carried out with a low flow pump and frequency regulation. The collection of

    solutions was made in two stages; during the first stage it was watered to the extraction of the

    copperoxides inopencircuit.The fourthday,aclosedcircuit irrigationbeganwithrichsolution

    return.Sampleswerecollected in flasksata fixedvolumeof30cm3. Ineach sampling,chemical

    analyses were made so as to determine total Cu and Fe and measurements of pH and Eh. The

    volume of each sampling of rich solution in the phase of open circuit was measured. In the re

    circulation phase, a volume of 10 L kept constant, calculating thebalance of copper fines. The

    temperature(30C)inthecolumnwasregulatedbyaheatingbelt.Copperandironcontentswere

    determinedbymeansofspectrophotometerofatomicabsorption.

    Isolationofbacteriafromthemineral

    Todetectthepresenceofbacteriainthemineral,5gofmineralsampleweretakenfromthecolumn

    andplacedinsterileErlenmeyerwith100cm3ofbasalmediumcontaining3g/LFeSO4.Thebasal

    culturemediumhadthefollowingcomposition:0.4gMgSO4*7H2O,0.056gK2HPO4*3H2Oand0.4

    g/L (NH4)2SO4, adjusted to pH 1.6 with concentrated H2SO4. The flasks were incubated in an

    environmentalshakerat30C.Thecultivationsolutionsweremonitoredperiodicallytodetermine

    pHandEh.Whenferrous ironbacteriaweredetectedbythe increaseofEh,10cm3ofthisculture

    wereusedtodetectsulphuroxidisingbacteria;thismediumcontainedpotassiumtetrathionate10

    mM inabasalmediumspecific to thisbacteria:6g (NH4)2SO4,1gMgSO4*7H2O,0.02gCa(NO3)2,

    and0.2g/LKClacidifiedtopH3.5withconcentratedsulphuricacid[8].Theseexperimentswere

    monitoredforsomedaystodeterminepH.Allexperimentswerecarriedoutinduplicate.

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    RESULTSANDDISCUSSION

    Parametersvariationintheexperiment

    ThevaluesofpHkeptclosetotwoasshowninFigure2.Duringthelastphaseofthetest,thepH

    descendedto1.7soastoallowthedevelopmentofmicroorganismsironoxidisingATandAF.

    Figure3showsthatthevariationofpotential(vs.SHE)valuesgoupastimeadvances,obtaininga

    close peak of 550 mV, a fact that would show iron oxidisingbacteria in the column filled with

    mineral.Itwaspossibletokeepthetemperatureofthesolutionbetween25Cand30C(Figure4),

    theoptimalgrowingtemperatureforthesemicroorganisms.

    As itcanbededucedbyobservingFigures5and6,copperoxideextraction isquicklyproduced

    with the already known kinetic when confronted to the action of sulphuric acid. After this, the

    curveofextractionvs.timeagreeswithkineticsofchalcopyriteinferricoxidation,asitisdescribed

    inthefollowingequation:

    CuFeS2+4Fe3+ Cu2+ +5Fe2++25 (1)

    Underthisequation,practically50%isextractedquickly,apercentageagreeingwiththepresented

    test,inwhich48%ofextractionofcopperwasobtainedin60hofleaching,(Figure1).

    Figure1Extractionofcopperandiron

    Figure2VariationofpHduringtest

    010

    2030405060708090

    100

    0 10 20 30 40 50 60 70 80 90

    %Cuy%Fe

    Time (days)

    Extraccin Cu (%)

    Extraccin Fe (%)

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    Figure3 VariationofpotencialredoxintheisolationsolutionsofFeoxidisingbacteria

    Afterthreedaysof leaching, itwasconsideredthattheextractedcopperoxidisedandthesample

    onlycontained

    copper

    in

    sulphur

    form.

    The

    seventh

    day,

    basal

    culture

    medium

    9K

    without

    ferrous

    sulphate was added, because it was considered that the sample contained iron in high

    concentrations,accordingtomineralogy.

    Figures1,5and6showafivepointjumpintherecoveryinonlyfourdaysofoperation.Thisfact

    agreeswiththebacterialactioninexponentialgrowth.Afterthisperiod,theextractionphasebegan,

    whichcanalsobeseeninthegraphics:9.61%extractionwasgivenina60daysperiodoftime.

    Figure4Variationoftemperatureofsolution

    Figure5Extractionphasesofcopper.Solublecopperbyacidleachingandcoppersulphurbybacteriaaction

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    Copperextractionforbioleachingcanbeestimatedina14%foranapproximate80daysperiodof

    time, as the total extraction comes from the 64.68 % for an approximate time of 90 days. It is

    consideredthatthisvaluedoesnotcorrespondtothetotalpossiblerecovery,becausethetestwas

    stoppedbeforethecurvereachedtheplateau.Consequently,ahigherrecoverycouldbeexpectedin

    anextendedperiodoftime.

    Thisphaseoflowerextraction,represented inFigure5,wouldbeso,duetotheformationof iron

    sulphateprecipitates(likejarosites),producingpassivationofthesurfaceofchalcopyrite,becoming

    a barrier for the solution in the process of diffusion, delaying the contact of these with the

    chalcopyritecrystalsandthedesorptionoftheproducttothesolution.

    Figure6 Copperrecoveryvs.rateofdeleaching

    Figure7 VariationofpotentialredoxintheisolationsolutionsofFeoxidisingbacteria

    Figure8 pHvariationintheisolationsolutionsofsulphuroxidisingbacteria

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    Apossibilitytoincrementthekineticsfordissolvingcopperinthelowgrowthphasewouldbeto

    produceremilling,oncethe fastkineticsphase isfinished(60h forthis test)and toreinitiatethe

    treatment, which would be in stages that would reduce the times of leaching here exposed.

    However, remilling related costs are sometimes prohibitive, taking into account that the new

    kineticswillcorresponditselfagaintotheonegiveninthepreviousphase,repeatingtheprocess.

    Presenceofbacteriainthecolumn

    Figure7showsavariationofredoxpotentialofthesolutionofironoxidisingbacteriaisolatedfrom

    the mineral. In approximately 15 days, Eh reached 600 mV (vs. Ag/AgCl), a fact indicating the

    presence of iron oxidisingbacteria, very probablyAcidithiobacillusferrooxidans and Leptospirillum

    ferrooxidans.ThisisprobablyduetothehighEhreachedattheendofexperiments(about700mV).

    Assoonasredoxpotentialreached700mVinthesolutionsofcultureofironoxidisingbacteria,

    therewasan inoculumofthesebacteriaputtoaspecificculturemediumforthedevelopment

    sulphuroxidisingbacteria.TheresultsobtainedinthistestshowthatthepHdecreasedevento

    1.5, which indicates the probable presence ofAcidithiobacillusferrooxidans andA. thiooxidans

    (Figure 8). Both bacteria generate sulphuric acid from the oxidation of reduced sulphurcontainedinthetetrationate.

    CONCLUSIONS

    Theresultsobtainedinthisworkevidencethatthemineralutilisedinthisstudyclearlycontained

    ironand sulphuroxidisingbacteriadevelopedwhenpHconditions, temperatureand iron in the

    solutionofirrigationenabledtheirdevelopment.

    Inbioleachingteststherewasanaverageof45%copperrecovery;33%correspondtotheleaching

    oxidesand12%isattributabletothesulphurbioleaching.

    Dependingon

    the

    obtained

    results,

    it

    can

    be

    concluded

    that

    it

    is

    possible

    to

    apply

    the

    bioleaching process to these ores, considering the low recoveries obtained for this mineral

    withthe flotationroutes.

    REFERENCES

    Watling, H.R, (2006). The bioleaching of sulphide minerals with emphasis on copper sulphides A review.

    Hydrometallurgy84,pp81108.[1]

    Jordan,H.,Sanhueza,A.,Gautier,V.,Escobar,B.&Vargas,T.(2006)Electrochemicalstudyofthecatalyticinfluence

    ofSulfollobusmetallicusinthebioleachingofchalcopyriteat70C.Hydrometallurgy83,pp5562.[2]

    Petersen, J. & Dixon, D.G. (2006). Competitive bioleaching of pyrite and chalcopyrite. Hydrometallurgy 83,

    pp4049.[3]

    Plumb,J.J.,McSweeneyN.J.&Franzmann,P.D.,(2008).Growthandactivityofpureandmixedbioleachingstrains

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    Rossi,G.(1990)Biohydrometallurgy,McGrawHillBookCompanyGmbH.UniversityofCagliari,Italy.[7]

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    W.C.Cooperb,S.K.Young.Hydrometallurgy88,pp.318.[10]

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