BiochemicalEngineeringJournal62 (2012) 48–55
ContentslistsavailableatSciVerseScienceDirect
Biochemical
Engineering
Journal
j o u r n al hom ep ag e :w w w . e l s e v i e r . c o m / l o c a t e / b e j
The
effects
of
fluoride
and
aluminum
ions
on
ferrous-iron
oxidation
and
copper
sulfide
bioleaching
with
Sulfobacillus
thermosulfidooxidans
Tácia
C.
Veloso,
Lázaro
C.
Sicupira,
Isabel
C.B.
Rodrigues,
Larissa
A.M.
Silva,
Versiane
A.
Leão
∗UniversidadeFederaldeOuroPreto,DepartmentofMetallurgicalandMaterialsEngineering,Bio&HydrometallurgyLaboratory,CampusMorrodoCruzeiro,s.n.,Bauxita,OuroPreto, MG,35400-000,Brazil
a
r
t
i
c
l
e
i
n
f
o
Articlehistory:
Received11November2011 Accepted7January2012
Available online 14 January 2012
Keywords:
Batchprocessing Thermophiles Growthkinetics Fluoridetoxicity Aluminumcomplexes Wastetreatment
a
b
s
t
r
a
c
t
MicroorganismsthatgrowathightemperaturescanimproveFe(II)bio-oxidationandtherebyits
tech-nologicalapplications,suchasbioleachingandH2Sremoval.Conversely,elementspresentinindustrial
growthmedia,suchasfluoride,caninhibitbacterialgrowthandironbio-oxidation.Inthiswork,the
influ-enceoffluorideonthekineticsofferrous-ironbio-oxidationwithSulfobacillusthermosulfidooxidanswas
investigated.Theeffectsoffluorideconcentrations(0–0.5mmolL−1)onbothironoxidationandbacterial
growthrateswereassessed.Inaddition,theeffectoftheadditionofaluminum,whichwasintendedto
complexfreefluorideandreducetheconcentrationofHFthroughtheformationofaluminum–fluoride
complexes,wasalsoinvestigated.Theresultsshowthat0.5mmolL−1NaFcompletelyinhibitedbacterial
growthwithin60h.Nevertheless,fluoridetoxicitytoS.thermosulfidooxidanswasminimizedbycontrol
ofthealuminum–fluorideratiointhesystembecause,ata2:1aluminum–fluoridemolarratio,bacterial
growthwassimilartothatobservedintheabsenceoffluorideions.Despiteaslowerbacterialgrowth
rate,fluorideconcentrationslessthantheinhibitoryconcentrationincreasedtheFe(II)oxidationrate.
Successfulcopperbioleaching(80–100%)fromfluoride-containingsulfideores(1%totalfluoride)was
demonstratedinthepresenceofaluminum.
© 2012 Elsevier B.V. All rights reserved.
1. Introduction
Ferrous-ironbio-oxidationhasmanytechnologicalapplications, includingbioleaching[1], whereferriciron accountsfor sulfide oxidation.MostFe(II)bio-oxidationstudieshavebeenperformed withmesophilicmicroorganismssuchasAcidithiobacillus
ferroox-idans [2] and Leptospirillum ferriphilum [3], although moderate
thermophiles and extreme thermophiles can positively impact bioleachingbecauseoffaster sulfideoxidationathigh tempera-tures.Theelectronpathwayfromferrous-irontooxygenhasbeen proposedtoincluderusticyanin in A.ferrooxidans [4] andRuBP carboxylasesinSulfobacillus[5].
ThegrowthmediumcanstronglyinfluencetheFe(II)oxidation ratebecauseindustrial solutionsmaycontainaplethora of dis-solvedelements.Duringheapbioleaching,forexample,thegangue mineralscanenrichtheleachsolutionwithelementsthatare harm-fultothebacteria,thusimpairingferrous-ironoxidationkinetics [6]. Ojumu et al. [7] have shown the effect of increased ionic strengthonmesophilicbacterialgrowth.Inadditiontoreducing
∗CorrespondingauthorTel.:+553135591102;fax:+553135591561/1596.
E-mail addresses: versiane@demet.em.ufop.br, versiane.ufop@gmail.com,
va.leao@uol.com.br(V.A.Leão).
dissolvedoxygenconcentrations,ahigherionicstrengthreduces free waterconcentration,and thebacteria therefore losewater becauseofosmoticeffects[8].AnionsaffectFe(II)andsulfur oxi-dationdifferently,butnitrateandchloridearethemostimportant inhibitorsofmesophilicbacterialgrowth[9].Suchspeciesreduce thetransmembranepotentialandenableH+ crossingofthecell membrane,therebyloweringtheinternalcellpHandimpairing growth[10].Anotherinhibitionmechanismhasbeenproposedfor speciessuchasHF,whichareelectricallyneutralatthepHvalue wherebioleachingoccurs.Afailureofaheapbioleaching opera-tionduetothepresenceoffluorideionsontheorehasrecently beenreported[11],andthisphenomenonwasexplainedbythe fluoridechemistry.AtthelowpHlevelsofbioleachingoperations, fluorideionsareconvertedintoHF,which,unlikeF−,canpenetrate thecellmembraneanddissociateintoH+andF−.Theinternalcell pH,whichisneutral,isthenloweredbyH+,whereasfluoride com-bineswithsomeenzymes.Theoverallresultistheinhibitionof bacterialgrowth[8],and,therefore,theinhibitionofferrous-iron oxidation,irrespectiveofthebacterialstrain(mesophiles, moder-atethermophilesorextremethermophiles)[12,13].
Inbioleachingoperations,inorganicweakacidssuchasHFmay bepresentintheleachingliquordependingontheoremineralogy. Becausetheprocessingoforesandconcentratesthatcontainhigh contentsofimpuritiesarebecomingcommonplace,theindustryis
1369-703X/$–seefrontmatter© 2012 Elsevier B.V. All rights reserved.
facingthechallengeofdealingwithsuchspecies,whichare some-timespresentinhighconcentrations[14].Meanwhile,bioleaching by moderate thermophiles has been studied because sulfide oxidationisfasterandbecausethesemicroorganismsarefoundin heapleachingoperations,wheretheheaptemperatureishigh.
Theeffectsoffluorideionsonthegrowthrateofbacteria rele-vanttobioleachinghavenotbeenextensivelyaddressed.Fluoride effectsareknowntobeovercomebythepresenceofaluminum. However,theeffectsoffluorideandaluminumonbothbacterial growthand Fe(II)oxidation bySulfobacillusthermosulfidooxidans havenotyetbeenquantified.Inaddition,noconsensushasbeen reachedregardingthemainaluminum–fluoridecomplexesformed duringbioleachingoffluoride-containingores.WhereasDopson etal.[12]andSundkvistetal.[13]havesuggestedAlF2+asthemain complex,BrierleyandKuhn[11]haveproposedAlF2+asthe pre-dominantspecies.Therefore,thispaperwasundertakentoassess theimpactoffluorideionsonferrous-ironoxidationbymoderate thermophiles.
2. Materialsandmethods
2.1. Ferrous-ironbio-oxidationexperiments
S. thermosulfidooxidans (strain DSMZ 9293) was grown in a
mediumcomposedof0.4gL−1(NH
4)2SO4,0.8gL−1MgSO4·7H2O, 0.4gL−1K
2HPO4,2.5gL−1ferrous-iron(FeSO4·7H2O)and0.1gL−1 yeastextract, at pH1.5. Thecells were maintainedthroughout the experiments in an orbital shaker (New Brunswick Scien-tific),at 50◦C and 200min−1 and wereused astheinocula for the bio-oxidationexperiments when the potential reachedthe 580–600mV(Ag/AgCl)range.
Thebio-oxidationexperiments(duplicate)wereperformedin abaffledbioreactor(NewBrunswick Scientific,BioFlo110)with 2Lofsuspensionthatcontained10%(volume)oftheinoculum.To producethesuspension,200mLoftheinoculum(notpreviously adaptedtoeitherfluorideoraluminum)wastransferredfromthe shakertothebioreactor,andgrowthmedium(supplementedwith yeastextract)wasaddedtoproduceafinalsolutionvolumeof2L thatcontainedbetween5×106and5×107cellsmL−1.ThepHwas manuallyadjustedto1.5and keptat thisvaluethroughoutthe experiment.ApHmeter(Hanna2221)andglass-membrane elec-trodecalibratedagainstpH4.0and7.0buffersolutionswasused forthepHmeasurements.ThepHwascontrolledduringthe experi-mentsbytheadditionofeitherconcentratedsulfuricacidorsodium hydroxide solution.Thetemperatureand thestirringratewere maintainedat50◦Cand300min−1 (dualRushtonimpeller,5cm diameter),respectively.Thisstirringratewasdefinedasthevalue thatproducedthehighestferrous-ironoxidationrate[15].Aeration wasprovidedbyoil-freecompressorsatarateof1Lmin−1,and 5mLsampleswereregularlywithdrawnandanalyzedfor ferrous-ironconcentrationandcellcounts.NoadditionalCO2wasaddedso thattheyeastextractwasthemaincarbonsource.
In the bioreactor experiments, both bacterial growth and ferrous-ironoxidationwereassessedinexperimentswhere fluo-rideions(NaF)wereadded.Fluorideconcentrationswerevaried from0to0.50molL−1(0–10mgL−1),inthepresenceandabsence ofaluminum(Al(OH)3)sothatthefollowingAl:Fmolarratioswere achieved:0.0:0.13;0.0:0.25;1.0:0.50;2.0:0.5and3.0:0.5,3.0:0.0.
2.2. Bioleachingexperiments
Coppersulfidebioleachingexperimentswereperformedwith twosecondaryores.Thefirstsamplecontained0.99%copper (high-grade ore), and the second contained0.73% copper (low-grade ore).Mineralogicalanalysisperformedbyopticalmicroscopyand
SEM–EDS indicated that thehigh-copper ore sample contained biotite(42.3%),magnetite(21.5%)andsilicates,especially amphi-bole(18.9%) and garnet (6.9%).In addition, thelow-copper ore containedapproximatelythesameamountofbiotite(34.9%)and amphibole(25.2%),lessmagnetite(9.5%)andmoregarnet(16.7%). Thecopper-containingmineralscomprisedbornite(36%)aswell aschalcocite(64%)inthehigh-copperore,whereasthelow-copper orecontained39%bornite,55%chalcociteand6%chalcopyrite.Both oresalsocontained0.58–0.73%chlorideand0.53–0.75%fluoride aseitherfluorite(CaF2)orfluoride-containingsilicates.Theiron andaluminumcompositionswere27.8%Feand5.0%Alinthe low-copperoreand33.7%Feand3.9%Alinthehigh-coppersample.
Thebioleachingpotentialofbothoreswasassessedin250mL Erlenmeyerflasks.Avolumeof50mLofthegrowthmedium (sup-plementedwithyeastextract)wasadjustedtotherequiredpHand transferredtotheflasks.TheamountofrequiredFe(II)wasadded asanacidsolutionthatcontained50gL−1Fe(II)(asFeSO4·7H2O). Afterwards,5goftheore(correspondingto5%(w/v)pulpdensity) wereadded,andtheflaskswereinoculatedwitha10mLaliquot ofthebacteriathatcontained1×107cellsmL−1.Finally,sufficient distilledwaterwasaddedtodilutethefinalslurrytoavolumeof 100mL.ThepHwassubsequentlyadjustedtotherequiredvalue (1.65),andtheflaskweightwasrecorded.Unlessotherwisestated 350mgL−1 and200mgL−1 Al(asaluminumsulfate)wereadded tothebioleachingtestswiththehigh-andlow-gradeores, respec-tively.Atemperature-controlledorbitalshaker(NewBrunswick) provided mixing(at200min−1).Eachflaskwassampledbythe removalofa2mLaliquotoftheleachsolution,whichwasthen used for elemental analysis. The redox potential (Digimed) (vs. Ag/AgCl reference)wasrecorded.Evaporationlosseswere com-pensatedbytheadditionofthegrowthmediumtotherecorded weight.Sterilecontrolswerealsoruninthepresenceof0.015% (v/v)methylparaben–0.01%(v/v)propylparabensolutionsasa bac-tericide.
2.3. Analysis
Cell countswere performedusinga Neubauer chamberin a light-contrast microscope (Leica). Aluminum and fluoride were analyzedbyICP–OESandionchromatography,respectively. Fer-rous ion wastitrated againsta standard potassiumdichromate solutioninthepresenceofa1H2SO4:1H3PO4solutionusingan automatictitrator(Schott-TritolineAlpha).Allchemicalsusedin thisstudywereanalytical-gradereagents(AR)unlessotherwise stated,andallsolutionswerepreparedwithdistilledwater.
StatisticalanalysiswasperformedusingtheOriginTMversion8.0 softwareprogramtodeterminethespecificgrowthrate,theFe(II) oxidationrateandtheyieldvaluesfora95%confidenceinterval. Thedatapointsusedtocalculatesuchparameterswerethosethat producedlinearregressionwithcorrelationcoefficients(r2)greater than0.95.
3. Resultsanddiscussion
3.1. Ferrous-ironbio-oxidation
[17].Inthelag-phase,growthisessentiallyzerobecausecellsare adaptingtothenewenvironment,andnewenzymesandstructural componentsarebeingproduced.Afterthelag-phase,the bacte-rialpopulationstartstoincrease (growthphase); eventually,as nutrientsbecomedepletedorinhibitoryproductsaccumulate,the stationaryphaseisattained[17].Fluorideionshavebeenshown toimpair thegrowthof different bacterialstrains[18], includ-ingmesophilicbioleachingmicroorganisms[19].Thisresultwas alsoverifiedinthepresentworkforthegrowthofthemoderate thermophileS.thermosulfidooxidansinferrous-iron.Nobacterial growthwasobservedwithin60hduringFe(II)bio-oxidation exper-imentsperformedwith0.50mmolL−1 (10mgL−1)totalfluoride. ThisdetrimentaleffectwasobservedbecauseHFisaweakacid (pKa=3.2,at25◦Candinfinitedilution)thatexistsprimarilyasHF (98%ofthefluoride-containingspecies)atthepHutilizedinthis study(1.5). HFisa highlypermeantsolute,witha permeability throughlipidbilayermembranesthatissevenordersofmagnitude greaterthanthat ofF− [20].In acidophiles,althoughthe exter-nalsolutionisacidic,thecytoplasmicpHisneutral becausethe cytoplasmicmembrane,despiteallowingthepassageofionsand moleculestosupportmetabolism,hindersprotonsfromentering thecell.Theentryofprotonsisreducedbyaninverted transmem-branepotential(),whichcontributestotheneutralcytoplasmic pH[21].Small, uncharged molecules suchas HFcan cross the cellmembrane.Afterenteringthecell,HFdissociatesintoH+and F−,whichdecreasestheinternalpHandaffectsmicrobialgrowth accordingly[8].Growthisalsoimpairedbecausefluorideitselfcan inhibittheactivityofmanyenzymes[18].
Thedetrimentaleffectposedbyfluorideonbacterialgrowth canbeovercomebytheadditionofaluminumtothesystem[19], asdepicted in Fig. 1.Fig. 1 shows no lag-phasein the experi-mentperformedwithouteitherelement(blank).However,growth wassomewhataffectedinthepresenceof0.5mmolL−1 fluoride and2mmolL−1aluminum(Al/F=4)andalag-phasewasobserved. Whenthealuminumconcentrationwasincreasedto3mmolL−1 atthesamefluorideconcentration(Al/F=6),thislag-phase disap-peared,whichpointstothedetoxificationeffectofaluminumon fluoridetoxicity[11,12].
Attheendofthelag-phase,thebacteriaareadaptedtotheir environment,andcelldoublingstarts(theexponentialphase).If growthisnotlimited,doublingwillcontinueataconstantgrowth rate,whichcharacterizestheexponentialgrowthphase,inwhich celldoublingwillcontinueattheso-calledspecificgrowthrate(). Thisgrowthphaseappliestoclosedsystemswheregrowthisthe
0 3 6 9 12 15
15.0 15.5 16.0 16.5 17.0 17.5 18.0
blank R2 = 0.99
Al/F = 6 R2 = 0.99
Al/F = 4 R2 = 0.98
Ln (bacterial population)
Time (days)
Fig.1.BacterialcountsasafunctionoftimeforthegrowthofS.thermosulfooxidans
onFe(II)atdifferentAl/Fmolarratios.[Fe2+]
0=2.5gL−1,50◦C,10%inoculum,pH1.5,
300min−1,[F]
total=0.5mmolL−1.Blankexperiment:[Al]t=[F]t=0.
0.0:0.0 0.0:0.130.0:0.25 1.0:0.5 2.0:0.5 3.0:0.5 3.0:0.0 0.05
0.10 0.15 0.20 0.25 0.30 0.35
Specific grow
th rate (h
-1 )
Al:F molar ratio
Fig.2.Effectoffluorideandaluminumadditiononthespecificgrowthrate() duringFe(II)oxidationbyS.thermosulfidooxidans.Experimentalconditions2.5gL−1
Fe2+;0.1gL−1yeastextract;Norrisgrowthmedium,pH1.5;300min−1and50◦C.
onlyprocessthataffectscellconcentration(X)[17].AplotoflnX versustimegivesastraightlinewithslope()(Fig.1).
Thespecific growthrate ()wasdetermined frombacterial countsperformedinthebioreactor(Fig.2).Thespecificgrowth rate(0.283±0.035h−1)calculatedfortheexperimentperformed intheabsenceofbothfluorideandaluminum(blank)isconsistent withpreviousstudiesonFe(II)oxidation byS. thermosulfidooxi-dans(0.220±0.025h−1)[15].Themaximumspecificgrowthrate (max)wasdeterminedforthisbacteriumgrowninthepresence of2–20gL−1Fe(II)andthevalueof0.242h−1wasobserved[15].
As shown in Fig. 2, the presence of fluoride ions reduced the specific growth rate. At a total fluoride concentration of 0.125mmolL−1, was reduced to 0.128±0.037h−1, i.e., less than half thevalue observed in theabsence of the anion. The specificgrowthrate wasfurtherdecreased to0.085±0.028h−1 forhigherfluorideconcentrations(0.25mmolL−1),whichreflects the inhibitory effect of HF onbacterial growth [8]. When alu-minumwasalsoaddedtothebioreactor,itsdetoxificationeffect became evident.As already stated,no growthwasobserved in thepresenceof0.5mmolL−1(10mgL−1)totalfluoride.However, when 1.0mmolL−1 Al wasaddedtothis fluorideconcentration (Al/F=2),growthwasdetected,andaspecificgrowth-ratevalue of 0.091±0.034h−1 wasmeasured. Fluoride inhibition wasnot completelyovercomeatthisaluminumconcentrationbecausethe specificgrowthratewasstatisticallysimilartothoseachievedin theabsence of aluminum and at lower fluoride concentrations (0.125mmolL−1–0.25mmolL−1).Avaluesimilartothatproduced intheabsenceoffluoridewasachievedwhentheAl:Fmolarratio wasincreasedto4 (2.0mmolL−1 Al–0.50mmolL−1 F)(Fig.2). AfurtherincreaseintheAl/Fmolarratioto6(3.0mmolL−1 Al– 0.50mmolL−1F)resultedinasmallergrowthratethanwhenonly 3.0mmolL−1aluminumwaspresent.Thisparameterisagain sta-tisticallysimilartothatproducedwhennoneoftheelementswere present.TheanomalousgrowthrateobservedatAl/F=6maybe duetothepredominanceofunchargedaluminumfluoridespecies (AlF3),butthisresultrequiresfurtherinvestigation.
Thepositiveeffectofaluminumonbacterialgrowthinthe pres-enceoffluoridecanbeexplainedbyaluminum–fluoridecomplex formationEq.(1–4),whichproducesspeciesthatcannotcrossthe bacterialcellmembranes.
Al3++F−
⇆AlF2+ logˇ1= 7.01 (25◦C,I→ 0) (1)
Al3++2F−
AlF2+
AlF2+
AlF2+
AlF2+
AlF2+
AlF2+
AlSO4+
AlSO4+
AlSO4+
Al(SO4)2- Al(SO
4)2- Al(SO4)2
-0.000 0.200 0.400 0.600 0.800 1.000
2 4 6
Mol
a
r fr
acƟon
Al/F molar raƟo
Fig.3.Estimatedaluminumspeciation(molarfraction)inthepresenceofboth sulfateand fluoride ions. Conditions:25◦C, pH 1.50,infinite dilution (I→0). Totalconcentrations:0.5×10−3molL−1(fluoride);76.5×10−3molL−1 (sulfate);
44.8×10−3molL−1(ferrous-iron).Al3+,AlF
3andAlF4togetherrepresentslessthan
0.5%ofthealuminumspeciesandthereforedonotappearinthediagram.
Al3++3F−
⇆AlF3(aq) logˇ3=16.7 (25◦C,I →0) (3)
Al3++4F−
⇆AlF4− logˇ4= 19.4 (25◦C
,I→ 0) (4)
Thecompositionofthebio-oxidationsolution(aluminum,iron, fluoride and sulfate) wasused in a thermodynamicstudy per-formedtoestimatethedistributionofsolublealuminum–fluoride speciesinthesystem.Fig.3presentsthedistributionofaluminum complexesforthethreedifferentAl/Fmolarratiosstudiedinthe presentwork(atpH1.50andwith2.5gL−1Fe(II))at25◦Cand infi-nitedilution,withdataobtainedfromboththeNISTdatabase[22] andtheresultsofGimenoSerranoetal.[23].Valuesofstability constantsforthetemperatureandionicstrengthofthemoderate thermophileleachingcouldnotbefound.Therefore,actualvalues aresomewhatdifferent,butitisbelieved,however,thatthemain findingscanbeappliedtotheexperimentalconditionsstudiedhere. ThisanalysiscoversthebeginningoftheexperimentswhenFe(II) wasthemainironspecies,i.e.,ferricironconcentrationsweretoo lowtoaffectaluminum–fluoridespeciationortoformjarosite.For alltheAl/Fmolarratiosstudied,thecalculationsindicateAlF2+as thepredominantAl/Fcomplex,followedbyAlF2+(Fig.3);these resultsareconsistentwiththeworkofBrierleyandKuhn[11],who alsoindicatedAlF2+asthemainaluminum–fluoridecomplex dur-ingmesophilicbioleachingofsecondarycopperores.Nevertheless, AlF2+andAlF2+representmorethan97%ofthealuminum–fluoride complexes,andbothspecieslikelypredominateat50◦C.
Becausesulfatewasalsopresentinthereactor,Fig.3also sug-geststhatthecomplexesAlSO4+ andAl(SO4)−,whichrepresent between67%(Al/F=2)and85%(Al/F=6)ofthealuminumspecies, arealsoimportant.Thisresultis consistentwithprevious find-ings[13].Furthermore,theHFconcentrationwasdecreasedtoless than6×10−5molL−1,whichrepresentsonly12%ofthe fluoride-containing species (unlike the 98% observed in the absence of aluminum). Thedecreased HFconcentration positivelyaffected thebacterialgrowth.Insummary,fluoridecomplexationwith alu-minumreducestheHFconcentrationandpreventsfluoridefrom extensivelyenteringthemicrobialcell.
S.thermosulfidooxidansutilizesFe(II)asasubstrateforgrowth
[24]. Fig. 4 presents the Fe(II) profile in the experiments per-formedinthepresenceoffluorideandaluminum.Intheabsence ofaluminum(Fig.4a),increasedfluorideconcentrationsresulted inlongerdelays forthestartofFe(II)oxidation. Thistimespan
0 10 20 30 40 50 60 70 80 0.0
0.4 0.8 1.2 1.6 2.0 2.4 2.8
[F]tot = 0.50mmol/L
[F]tot = 0.25mmol/L [F]tot = 0.13mmol/L
[F]tot = 0.00mmol/L
(a)
[Fe
+2
] (g/L)
Time (h)
0 10 20 30 40 50 60 70 0.0
0.4 0.8 1.2 1.6 2.0 2.4 2.8
Al:
F = 0
(0.
5mmol.L
-1F
tot
)
Al:
F = 2
Al:
F = 6
Al:
F = 4
(b)
[Fe
2+ ] (g.L -1 )
Time (h)
Fig.4. Effectoffluoride(a)andAl:Fmolarratio(b)onFe(II)oxidationbyS. thermo-sulfidooxidans.Experimentalconditions2.5gL−1Fe2+;0.1gL−1yeastextract;Norris
growthmedium,pH1.5;300min−1and50◦C.In(b),fluorideconcentrationwasset at0.50mmolL−1.
matches the lag-phase period (datanot shown), during which growthwasnotexpressiveandthereforenosubstrate consump-tionwasobserved.At0.5mmolL−1fluoride,nobacterialgrowth was observed nor was Fe(II) oxidation detected.As previously discussed,ata fluorideconcentrationof0.5mmolL−1,the addi-tionofaluminumenabledbacterialgrowth(Fig.1)andsubstrate consumption(Fig.4b);theFe(II)concentrationwasconsequently reducedwithtime.
Theyield(Y)canbedeterminedfromthechangeinbiomass con-centration(X)andsubstrateconsumption(S)[25]andtheresults areshownTable1.Higheryieldvaluesimplybettersubstrate uti-lizationbythebacteria.Inalltheexperiments,theyieldwaswithin thesameorderofmagnitude(1010cellsg−1-Fe(II)),irrespectiveof theAl:Fmolarratio.Nevertheless,theyieldwaslowerwhenonly fluoridewaspresent,whichimpliesthatenhancedmetabolic activ-ityisrequiredtosustaingrowth[16].ForSaccharomycescerevisiae, theenergy requiredtoactivatetheplasma-membraneATPases,
Table1
Effectsaluminumandfluorideadditionsontheyieldcoefficient(Y)duringFe(II) oxidationbyS.thermosulfidooxidans.Experimentalconditions2.5gL−1Fe2+;0.1gL−1
yeastextract;Norrisgrowthmedium,pH1.5;300min−1and50◦C.
Aluminum(mmolL−1) Fluoride(mmolL−1) Yield(1010cellsg−1Fe(II))
0.0 0.00 5.30±1.00
0.0 0.13 2.83±0.12
0.0 0.25 3.06±0.74
1.0 0.50 –
2.0 0.50 3.62±0.75
3.0 0.50 5.03±0.65
Table2
EffectsaluminumandfluorideadditionsontheFe(II)bio-oxidationrate.
Experimen-talconditions2.5gL−1Fe2+;0.1gL−1yeastextract;Norrisgrowthmedium,pH1.5;
300min−1and50◦C.
Aluminum(mmolL−1) Fluoride(mmolL−1) Fe2+oxidationrate(gL−1h−1)
0.0 0.00 0.179±0.019
0.0 0.13 0.323±0.047
0.0 0.25 0.426±0.042
1.0 0.50 0.118±0.009
2.0 0.50 0.128±0.006
3.0 0.50 0.146±0.014
3.0 0.00 0.140±0.009
whichpumpprotonsoutofthecell,hasbeenshowntoresultin anincreaseintherespirationratewithadecreaseincellgrowth andthuscellyield[26].Slightlyhigheryieldvalueswereobserved inthe experimentswith aluminum—aconsequence of its posi-tiveeffectonbacterialgrowth(Fig.2).Theseresultsareconsistent withthoseobservedduringferrous-ironoxidationwithA. brier-ley in two different studies. Konishi et al. [27] determined an yieldvalueof2.05×1010cellg−1inthepresenceof2.0gL−1Fe(II), whereasNematiand Harrison[28]achieved5.38×1010 cellg−1 with1.8gL−1Fe(II).
Theferrous-iron consumptionrate(d[Fe(II)]/dt)isequivalent inabsolutetermstotheFe(II)oxidationrate,andthelatterwas determinedfromtheslopeofthelinearpartoftheferrous-iron concentrationprofileshowninFig.4aandb.Thisapproachwas selectedbecausethefirst-orderkineticsmodelproposedby Franz-mann[29]didnotproducegoodfitstotheexperimentaldata.The calculatedvaluesareshowninTable2.Theferrous-ironoxidation ratewasdeterminedas0.179±0.019gL−1h−1intheabsenceof bothaluminumandfluorideions(blank);thisvalueislowerthan thatobservedbyPinaetal.[15],whodeterminedanoxidationrate of0.292±0.034gL−1h−1 inasimilarexperiment.However,this lattervalueisconsistentwiththatreportedbyWatlingetal.[30], whoinvestigatedgrowthin10gL−1Fe(II)(∼0.12gL−1h−1).It is alsoconsistentwiththegrowthofA.ferrooxidans(0.14gL−1h−1) inthepresenceof2.5gL−1Fe(II)[28],and,asexpected,higherthan thevalueobservedfor A.brierleyi(−0.053gL−1h−1)in 1.8gL−1 Fe(II)[28].
TwoadditionalimportantoutcomescanbediscernedinTable2. First,aluminumcanovercomethedetrimentaleffectposedby flu-orideions duringFe(II) oxidation by S.thermosulfidooxidans, as alreadystatedinthediscussionthatcoveredthebacterialgrowth rate.However,in theexperimentswhere thecation is present, Fe(II)oxidationratesareslightlylowerthanthoseobservedinthe absenceofbothelements(blank).Similarfindingshavenotbeen observedforthisstrain,andinhibitoryeffectshavebeenreported onlyforhigheraluminumconcentrationsandother microorgan-isms. Blight and Ralph [31] have observed a reduction in cell numbersandduplicationtimeduringferrous-ironbio-oxidation ataluminumconcentrationsgreaterthan2.7gL−1foran unidenti-fiedmesophilicculture,whereasOjumuetal.[7]observed,during Fe(II)oxidationbyL.ferriphilum,deleteriouseffectsonFe(II) oxi-dationandbacterialgrowthonlyathighaluminumconcentrations (10gL−1).
Among the results in Table 2, the effect of low fluoride concentrations on the Fe(II) oxidation rates are also note-worthy. Although the presence of fluoride induced a longer lag-phase during bacterial growth (Fig. 1), iron oxidation was faster in the presence of fluoride (Al:F ratios of 0.0:0.13 and 0.0:0.25) as soon as the exponential phase began. Iron oxida-tionreacheda rateof0.426±0.042gL−1h−1 inthepresence of 0.25mmolL−1 fluoride, whereas the rate in the blank experi-mentwas0.179±0.019gL−1h−1).Apossibleexplanationforthis behavioristheneedtoactivatecellmetabolismasaresistance
mechanismtothepresenceoflowconcentrationsoffluoride[16], forwhichthegrowthrateisdecreasedandthelengthofthe lag-phaseisextended.Itisthereforeproposedthatthedecreaseincell internalpH(causedbyHFdiffusion)forcesthesystemtopump protonsout(increasedATPaseactivity)tobalancethediffusionof theHFmoleculesintothecell.Overall,theenergyrequirementsare increased,whichresultinanincreasedsubstrateconsumptionrate withoutanincreaseinbiomassyield,asobservedinotherstudies [32].
Becausefluoridetoxicitycanbeovercomebythepresenceof aluminumduringFe(II)bio-oxidationbyS.thermosulfidooxidans, bioleachingexperiments wereperformedwithtwocopperores thatcontainedfluorideintheirgangueminerals[14].
3.2. Bioleachingexperiments
Two different secondary copper sulfide ores that comprise mainlychalcocite,borniteandchalcopyriteasaminorphasewere bioleachedwithS.thermosulfidooxidansat50◦C inthepresence of1gL−1 Fe(II)toensureafastincreaseinsolutionpotential.An externalferrous-ironadditionwaslaterfoundnottoberequired becauseirondissolutionfromtheoresprovidedenoughsubstrate forbacterialgrowth[14].Bothsamplescontainedmorethan90% cyanide-solublecopper[14],i.e.,copperthatiseasilyamenableto bioleaching[33].Becauseoftheobservedrapidferrous-iron oxi-dationbythebacterium(Fig.4),asharpincreaseinthesolution potentialwasexpectedduringtheseexperiments.Nevertheless, althoughtherewassignificantcopperextractioninboththebiotic andabioticsystems,ferric-andferrous-ironconcentrationswere similar to those achieved in the control experiment (data not shown),andpulppotentialvalueswereneverhigherthan450mV (Ag/AgCl),asshowninFig.5.Similarresultshavebeenreported duringbioleachingof achalcopyriteorethatcontainedfluoride [6].These resultsshouldbe comparedwith, for example,those observedduringnickelsulfidebioleachingwiththesamestrain, wherepotentialsashighas600mV(Ag/AgCl)wereobserved[24]. Therefore, someharmful substance might have beenimpairing bioleaching.Fig.5alsoshowsdifferentcopperextractionsfromthe high-gradeoreforboththebiotic(100%)andabiotic(75%) experi-ments.Thisbehaviorwasalsoobservedwiththelow-gradeore,but withslightlyloweryields(80%and60%forthebioticandabiotic experiments,respectively),whichmightbeduetothepresenceof chalcopyriteinthelow-gradeore[14].
0 2 4 6 8 10 12 14 16 0
25 50 75 100
(a)
Copper extracƟon (%)
Time (days) pH=1.65 pH=1.65 Control
0 2 4 6 8 10 12
0 25 50 75 100
(b)
Copper extracƟon (%)
Time (days) pH=1.65 pH=1.65 Control
0 2 4 6 8 10 12 14 16 350
400 450 500 550 600 650
(c)
Eh (mV)
Time (days) pH=1.65 pH=1.65 Control
0 2 4 6 8 10 12
350 400 450 500 550 600 650
(d)
Eh (mV)
Time (days) pH=1.65 pH=1.65 Control
Fig.5.Copperextraction(a)and(b)andsolutionpotential(Ag/AgCl)(c)and(d)duringtheexperimentswiththehigh-grade(a)and(c)andlow-grade(b)and(d)copper oresintheabscenceofaddedaluminumions.Experimentalconditions:5%solids;75–53m;pH1.65;1gL−1Fe2+;200min−1,10%Norris(v/v),0.1gL−1yeatextractand 50◦C.
Aspreviouslyshown,aluminumcanovercomethe detrimen-taleffectsoffluorideonFe(II)oxidation,althoughtheamountof aluminumdissolvedfromtheoredidnotensuresuitable condi-tionsforbacterialgrowth.Therefore,anewseriesofexperiments wereperformedinthepresenceofanexternalsourceofaluminum,
i.e., 350mgL−1 and 200mgL−1 Al were addedto the bioleach-ing tests withthe high- and low-gradeores, respectively. This externalsourceofAlensuredanAl/Fmolarratioofatleast1.5 duringbioleaching,whichwasshowntoenablebacterialgrowth onferrous-iron(Section1)andtoincreasethesolutionpotentialto
0 4 8 12 16
0 25 50 75 100
(a)
Biotic
Abiotic
Copper extraction (%)
Time (days)
0 4 8 12
0 25 50 75 100
(b)
Biotic
Abiotic
Copper extraction (%)
Time (days)
0 4 8 12 16
300 350 400 450 500 550 600
Abiotic
Biotic
(c)
Eh (mV)
Time (days)
0 4 8 12
300 350 400 450 500 550 600
(d)
Biotic
Abiotic
Eh (mV vs Ag/AgCl)
Time (days)
600mV[14].Fig.6depictsthevaluesachievedforcopper extrac-tionsandthesolutionpotentialsforbothores.Inthepresenceof aluminum,thepotentiallevelsoutinthe500–550mV(Ag/AgCl) rangewithinfivedays.Thesepotentialsareapproximately150mV higherthanthevalueobservedinthecontrolexperiments(Fig.6c andd), whichconfirms thepredictionsof Sundkvistetal. [13]. Therefore,bacterialactivitywasconfirmed.Althoughfinalcopper extractionsweresimilarintheexperimentswithout(Fig.5)and with(Fig.6)theexternaladditionofaluminum,copperextraction wasfasterinthelattercase.Forexample,forthelow-gradeore, copperextractionswere70%and50%atthefourthdayofleaching inthepresenceandabsenceofaluminum,respectively.
Theresultsshowaclearincreaseinthelag-phaseperiodwhen fluoridespecies are present duringferrous-iron oxidation by S.
thermosulfidooxidans.Becausetheproductionofferricironisthe
mainbioleachingmechanism,theonsetofmetalextractionbecame excessively longer than expected or even did not occur [11]. Notwithstanding,sub-lethalfluorideconcentrationscandoublethe ferrous-ironoxidationkinetics,whichwillresultinfastersulfide oxidation.UnliketheFe(II)oxidation,bioleachingcanbeperformed atmuchhigherfluorideconcentrationsiftheorecontainselements suchasaluminumthatcancomplexfreefluorideandreducethe HFconcentrationintheleachingliquor.Ifthepresenceof fluoride-containingmineralsisdetected,extracaremustbetakenduring bioleaching,especiallywhentheleachingsolutionisrecirculated, suchasin bio-heap-leachingoperations [19]. Althoughfluoride toxicitycanbereducedbythepresenceofaluminum,the ferrous-ironoxidationratebyS.thermosulfidooxidansisslightlydecreased inthepresenceofthecation.Therefore,thebuild-upofboth ele-mentscanleadtohighionic-strengthvalues,whichcanalsoaffect bioleaching.Under theseconditions,solutionbleedingwouldbe requiredtoreducethefluoridetoxicityaswellastheionicstrength sothatbioleachingcanbeperformedproperly.
4. Conclusions
AtthepHlevelstypicallyfoundinbioleachingoperations, fluo-rideionscanadverselyaffectthegrowthofS.thermosulfidooxidans becauseofthepredominanceofHFspeciesinsolution.The bac-terialspecificgrowthratewasdecreasedfrom0.283±0.035h−1 in experiments without fluoride to 0.085±0.028h−1 when 0.25mmolL−1totalfluoridewaspresent.Suchdetrimentaleffects canbeovercomebythepresenceofaluminum(1mmolL−1Al– 0.5mmolL−1F)whichformsAlF2+complexesthatreducetheHF concentrationand thefluoridetoxicity accordingly. This reduc-tionin toxicity resultsin specificgrowth-ratevalues similarto those observed in theabsence of both aluminum and fluoride. Despite the increase in the lag-phase period, sub-lethal fluo-rideconcentrationscatalyzeferrous-ironoxidation,whichreaches 0.426±0.042gL−1h−1with0.25mmolL−1totalfluoride.The pos-itiveeffectofaluminumonthebioleachingofcoppersulfideores that contain fluoride wasdemonstrated, and at least80% cop-perextractionwasachieved.Overall,forthoseoresthatcontain fluoride-containingminerals,bioleachingcanbeperformedif alu-minumsourcesarepresentoraddedtothebioleachingsystem.In heapbioleachingapplications,thebuild-upofaluminumand fluo-ridecanleadtofailuresduetohigh-ionic-strengthconstraints,and regularsolutionbleedingsmayberequired.
Acknowledgements
The financial support from the funding agencies FINEP, FAPEMIG,CNPqand CAPES is gratefully appreciated.The “Con-selhoNacionaldePesquisas”(CNPq)scholarshiptoV.A.Leãoisalso acknowledged.
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