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  • 8/10/2019 Donat - leaching.pdf

    1/18

    CHAPIER

    IO

    PRINCIPLES,

    MECHANISMS

    AND

    DYNAMICS

    OF CIIALCOCITE

    HEAP

    BIOLEACHING

    JOCHEN

    PETERSEN]

    AND

    DAVID

    C.

    DIXONT

    Dqafln.nt

    oJ

    Ch?

    i.at Ensinznihs.

    Uni{sitr

    of CaP?

    To\|

    '

    Pi

    de aas

    Ronlebosch

    7701

    S.u1h

    Alrica E

    tuil:

    iothen.Pete6e

    @u.t.a...a

    1

    Deparh.nt

    of

    Moktiah

    Ensineai

    s

    u ire$itt

    ol

    Btitish

    Cotunbid

    3A9

    ds1

    Stores

    Rand

    Vau)upr,

    B.C.

    V6T

    121.

    Canadd-

    E

    nail:

    di\an@i

    tcrcha\e

    ub.

    c4

    1.

    INTRODUCTION

    Heap

    laching

    is

    a

    well

    established

    nining

    technologv

    thal

    involves

    slacking croshed

    ore

    inlo

    piles

    constructed

    on

    an

    imperneable

    layer

    fitted

    with a sohrtion

    drainage

    syslem,

    ;r ananged

    on

    a

    slope

    to

    facilitate

    drainage.

    In manv

    cases

    the

    ore

    is

    agglomerated

    through

    tumbling

    with acid

    and/or

    inigation

    solution

    prior to stacking

    aolution

    is

    ilTigated

    (continuously

    or

    inlermittenlly)

    over

    the top surface

    of

    the

    heap

    and

    left

    1o

    sep through

    the

    ore

    bed where it

    can react

    with the targel

    minerals

    Dissolved

    metals

    are

    then

    tnnsported

    wilh the flowing

    solution

    to the

    bottom of

    the heap

    from

    wherc

    they

    are

    removed

    via

    the

    drainage

    sysiem

    into

    a

    collection

    pond

    as

    the

    pregnant

    leach

    solulion

    (PLS).

    The

    target

    metal

    js

    removed

    from

    the

    PLS

    tbrough

    a

    suitable

    lechnology

    (by

    solYenlextraction.

    cementation

    oradsorption).

    and

    ihe

    barcn

    solution

    (usually

    refered

    to

    as

    the raffinate)

    returned

    to the

    top

    surface

    of the

    heap'

    The

    technology

    has

    been

    in

    use since

    the 1960's

    for ihe

    acid

    leaching

    of

    copper oxide

    minerals,

    and since

    the

    1970's

    for the

    cyanide leaching

    of

    gold

    and

    silver.

    A

    related

    technology.

    dump leaching,

    is

    based

    on the

    same

    principtes

    as

    beap

    leachi.g,

    but usuatly

    uses

    uncrushed

    run-of-mine

    (ROM) mat'erial. usuallv

    coniaining

    sulfide mjnerals,

    or

    spent

    residue

    from leached

    heaps

    with

    a

    mineral

    grade

    too low

    to

    war-rant

    further

    processing.

    Anv

    additional

    metal

    liberated

    in a

    dump

    contributes

    to addilional

    revenue

    of

    tbe

    'nining

    operation.

    but

    dump

    leaching

    is

    rarely

    the

    primary

    method

    of

    metal

    extraction.

    It

    was in

    copper

    sulfide

    dump

    leach

    operations

    that

    the

    potential

    for

    bioleaching

    micro-organjsns

    was

    first

    realized

    (Bierley. 1997i Olson

    e,

    dl,

    2003). As

    the

    organisms

    inyolved

    occur

    naturally,

    no

    extemal

    intervention

    is

    needed

    to

    sustain

    193

    E.R.

    D.ndi

    a

    d ll Santl

    (etls.),

    Miu.bkl

    Pnr?s\ks

    oJ Mc,a/

    s,lrddr'

    193

    218'

  • 8/10/2019 Donat - leaching.pdf

    2/18

    l9l

    rlrl1

    R\trN

    /\Nt)

    rx\(,N

    rl(

    .:i,wtlr

    sUt\.1tr.,Ir.).tr...rt,hi,n,.u.triljr,,li,tIr(r

    \uttrt(IIrr.r.,t..r\,rt,r1Irrr)

    r'

  • 8/10/2019 Donat - leaching.pdf

    3/18

    196

    tlr

    RS|.N

    ,\Nt)

    txt()N

    l-lh

    r,,t..,r .r.r ..

    I tL.itr.t

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    hrDJ.

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    il:

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    cnerp\

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    h,sh.r

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    orumJnc

    acceterdrion

    of

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    ar

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    t::.1,_,l;

    ::

    ;;;;;;;,i.,;

    i

    jii'

    :l;.1,'l:;

    :I;::1,l;.l,1]:1

    :::l

    ;]

    :,i;

    ".1:,:'T,l::rll.:'":olidation

    reaclnn

    rrrhd,e

    been

    qejr

    ,e,edrcheJ

    (see

    ror

    ct

    ot..

    2006\.

    The

    o\)gen

    required

    ror

    rhi.

    reacrron

    .ome,

    rrom

    heap

    aerarion.

    rhe

    ,equired

    Jcrd.

    on rhe

    orher

    han,l.

    ,^,

    t"

    *rpr"a

    .iii.,

    "i

    i,

    the

    feed

    sorurion,

    or

    else

    rhrough

    the

    bio_oxidarion

    of py.i

    .

    "a;i;;;i

    i;if*,

    '.,

    (4)

    2FeS,

    +

    I50,

    +2H.O

    +

    2Fe2(SOr)r

    +2H,SO

    (s)

    2so

    +3or

    +2H:o

    +

    2H:soi

    -1l,l"lgl

    ln:

    l":,",*:oncernins

    rhe

    kinerrL\

    or

    bioreachins

    r\

    e\ren\,\e,

    mosr

    w,

    n

    ,u\,

    rncu.m

    on

    lant

    ler(hing

    pror

    esc,

    mrrnrained

    under

    con.lanr

    condilrons.

    :l

    i,Xp

    "i,,Tc.on.rhe

    orher

    hdnd

    man)

    pdrdmerer.,uch

    J,

    remperarure,

    oH.

    ll"

    r,

    llg

    (9.

    ","11, ,tiry

    dre

    nor

    wel.onrr.led

    .,nd

    may

    in

    ra.r

    ri,nr,

    .ii"l,.

    :::,:)1":,1*

    y.o

    r rre.

    rundJmenrar

    nuJy

    hr,

    been

    Jirecied

    dr

    aer".min,ng

    uio-

    o\roafton

    rrnetrc.

    under

    hedf

    cond

    ,on.

    rOtumu

    //

    a/. 2000,

    3.

    FUNDAMENTAL

    PRINCIPI,ES

    OF

    HIJAP

    BIOLEACHING

    l"lTj

    5:t

    ].ll

    n,*

    :ppeffs

    ro

    be

    a

    \eo

    ,impre

    proce*

    ,n

    concep,.

    rhe

    .ub-

    prc'esses

    riKrng

    price

    u ilhi

    rhe

    ore

    bed

    a, the

    ,oturion

    rnckles

    rhrougii

    rre

    rarher

    ::ll lin9

    rh:rr

    Tteraclions

    not

    yerrully

    undersro"a.

    o**,

    ai",i,gii,h;i*;.;

    processes

    ranging

    from

    the

    maffo-

    to

    the

    mn.

    ioi-*

    a

    p"i,*i',

    zooi;."

    -*

    "

    *

    "'c

    nxlro-scale

    as

    is

    illustfared

    in

    Fisure

    I

    Ar

    rhe

    macro

    scale,

    i.e.

    at the

    scate

    of

    the

    enlire

    heap.

    teaching

    is

    govened

    primarily

    hy

    rrirnspon

    ,,r

    muss

    und

    enerc i

    "..,,,..

    rvi-.

    "p..i,i."ri,';**

    ,;:,;,j:'"

    '|nro'

    rhrough.

    dnd

    ou,

    or

    rhe

    herp

    .

    Soluriun

    flow.

    tn

    uhflurared.

    coJr.et)

    granut:r

    pdrted

    hed,,oturion

    senera

    v

    ,,ow\

    J,ong

    lonuou.

    pJthsr)

    \

    but

    remrins:rrgninr

    i, p*-

    "",t.*, ".,i."*,

    Jni.lr,- Thi\

    ,trong\

    rnfluen,es

    heap

    [,ertormrnce

    rn

    lerm.

    otrex enr detircrv

    ano

    pro,luct

    remo al

    fiom

    the

    reicrion.ires

    w

    hjn

    lhe

    ore

    pafliclej

    .

    Hearfllu:He

    ot reJcrion.uhrchr.rgnrticJnrin.Ulrrdcteaching.isrr.rn.ported

    Ihroutsh

    rhe

    heap

    dotr

    nward

    asen,ibte-hear

    *

    rrh

    rh. no*i,s,,lrii._

    _a ,,,"*,.i

    d.

    larenr

    hezr

    \ irh

    rhe

    .,,s

    ot

    humid

    Jrr.

    D.p*.,,g

    ";;tr;;

    ,;;;;".i;;;

    i"_,i)

    h""p.

    .r,

    ,*rr.

    .enarn

    rempemrure

    rror.ire..

    ""a,"a"i,r.

    ."rirrl,i;""

    u|flc\e

    vrflrnre\

    ma)

    e\en

    alloq

    a reflain

    degree,,tc,,ntrot.

    .

    Ga,flos.

    qtthourh

    gi\

    flowi.u,uJjtl

    qe

    drrlbured

    inaerrredheno,.en{,nn,

    anprc .uppr)

    .t

    o\)gen

    rhruuchi,ut.

    rhe.

    ppjy

    or

    CO ,nJy

    hr

    r,iri,"a,,,.r.i

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    rn un.rerxr.J

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    lt11\

    ol

    rr,\rr

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    lll lll l,lrli)l

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    ]\(

    rrrN(l t

  • 8/10/2019 Donat - leaching.pdf

    4/18

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    and

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    i;H;l

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    leachrng

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  • 8/10/2019 Donat - leaching.pdf

    5/18

    11

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    Colunrn

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    lir

    &

    (.o-

    4

    Coluhn

    Ratfiide

    sotui;;

    53.57.

    47.2%

    ,;5;*i;;*;i#xi::r

    ;,"*

    Iiil

    j

    jl

    lr

    j;nlil

    H

    :;x[i

    ;lfl

    'ffi

    ,:l

    r

    fl

    [:1,';i."

    :1",:3

    i*fl

    ;,;;;,;;t"illLlt-""-^"";i:il':L***#t::',f

    :'".,,'.ti

    i{ffir*fffin';ila$,5ffi

    4.2.

    Chalcocite

    Leaching

    In

    Standard

    Laboratory

    Cotumns

    :J::::ilL:l;.';i.1,#:",1

    ',:f,,-."i:,,.,

    *

    tuyr

    nandird

    crpenmen.

    ,n

    a,,

    *+$.-*fi***

    rffi15*+#*+ffi*-

    bul

    rapidly

    i,creases

    to net

    Fe

    prodoction

    once

    the solution

    potential

    begins

    to

    increase.

    This

    is a slrong

    indication

    ihat

    some

    pyrite

    leaching occurs

    in

    parallel wilh

    chrlcocite lclching. F

    rther

    evidence can be

    tbund in

    the

    declining

    pH

    at

    the later

    (ages

    oflhe expcrimcnt.

    rpFoaching the feed

    pH

    of

    1.2. Although

    there

    is not

    net

    acid

    generntion.

    this trend

    is nonelhcless

    a

    clear indication thai

    acid

    is produced

    in

    the

    column,

    couDter

    balancing

    the

    bio-oxidation reaciion

    (l).

    which

    consumes

    acid

    at

    all tincs.

    This acid

    is either

    generared

    tiom

    secondary

    oxidation

    of

    elenental

    sulfu

    (produced

    from the stage 2

    chalcocite reaciion

    (3)).

    or from

    pyrile

    oxidation,

    or both.

    All other standard

    column

    experimenls

    exhibited similar behavior,

    with

    pH

    ;D

    some

    cases eventually

    falling

    belo$, thc

    feed

    level.

    The

    8

    column slaDdard

    experimeni

    was sei up specifically to

    investigate

    the

    prosression of dissolved constiluents

    (acid,

    Fe(II), Fe(III)

    xnd

    micro-ors:rnism, in

    the solutjon as

    it

    flows

    down

    the

    column lhrcugh analyzing

    samples

    in lhe

    interim

    cups. The

    profiles

    ofpH.

    solution

    potential

    (vs.

    Ag/AgCI) and

    microbial counis are

    shown

    ir Figure

    ,l.

    The

    expe ment was slopped after

    21 days.

    just

    as

    the wave

    of

    chaDges

    in

    solution

    potential

    began

    1o break

    ihrough

    (he

    last column, io

    allow

    analysis

    of

    the

    solid

    residues.

    The

    pH

    profiles

    clearly show two

    waves. oDe

    early

    peak

    moving through ihe

    columns

    duriDg

    dals

    I 7 and

    onc nuch brcader wave

    passing

    through belween days

    8 and 20.

    with peak levels increasing

    film column io column

    (pH

    1.4 in column I

    to

    2.5 in

    column

    8).

    In

    ea.h.olunrn,

    v,lution potentixls linger

    al

    low

    levels around

    380

    rnv

    ,r.

    Ag/AgCI

    li,

    somc

    rimc hcforo rnpidly rising 1() very high

    levels around

    700

    mV r. Ag/AgCl.

    This

    polLarli.l

    rise

    prcgresses in a wave lhrough

    the columns

    rt r mr. of

    rhout

    :10 cnr

    (i.e

    (n)c

    colunrn)

    cvcry 2 dals.

    Baclerial counts

    aiso

    indicnlc thLrl

    lhc

    nri.($irl p()tnrhli(nr

    progrrssc

    lhft)ugh lhc cohmns

    in

    n Iiont.

    rilh h,r.rL]iul nnnrb.rs r;sirrr

    ro l.vrlt.r,rsi(lcr.(l

    rhrivins

    (>10/

    crivc cells/nL)

    in llr

    rt)t).r

    (ohrnnrs

    lirsl

    h.lin. ll

    v

    t)r(r.r(l

    lil

    lhc,

    (,own

  • 8/10/2019 Donat - leaching.pdf

    6/18

    202

    PBTERSEN

    AND

    DIXON

    5

    I

    b)

    t

    a

    g

    *

    3.5

    1.0

    2,5

    2.0

    1.5

    1.0

    0.s

    0_0

    800

    7@

    600

    s00

    400

    300-

    20

    @

    120

    20

    @

    \20

    3.0

    2.5

    2.0

    1_0

    0.5

    0,0

    60

    100

    5''Ji'iJH.mf'

    """ad

    6,"e

    exlerimor

    a)

    Fe cotrenidioD.

    b)

    lorurion

    po.ntiar.

    d

    PRINCIPT,US Or

    (,ll^tr'(X'lTll

    IIEAP B|OI-UACIINO

    2t)3

    \

    Figzr. 4.

    Rdtrlls

    fron 8{olumn shd,rd .xp.riment )

    pH prcgEsion:

    b)

    solutio.

    pol.ntial

    prcsEssion;

    c)

    prosrsion

    of

    mimbial counts

    in

    slution

    t

    e

    s

    *

    5

    ?

    ,*.*

    E

    E

    '.oE+06

    E

  • 8/10/2019 Donat - leaching.pdf

    7/18

    2t0

    ?

    a

    150

    E

    .:

    90

    +

    Brcnrirl

    brm(rJn

    ongh

    1+-

    micrubiat

    btorhtroustr

    .rl ),t

    tlirNrllr\i,l

    r

    rl,\lr

    rr lll lllrAl'lr(,llA(lllN{i

    llll.tistN

    /\N,)

    tn\(

    )N

    ,.iA,ap

    5,

    Mictubjar.

    rH

    and

    poEnrixl

    progression

    nr

    erpen,ne

    25

    .

    The

    progrc..Jon

    or

    tH.

    porenllJl

    drd

    micro

    orSJni\m\

    are

    cleJrt\

    ret:Icd.

    Ficu,r 5

    pto,,

    rh(

    prosresinn

    u irh

    Jep,h

    Jnd

    ume

    or rh;

    n.ak

    ;H

    ;i;;,,.:;;;;:,"".

    ih"

    points

    where

    the

    solution

    pore,tiar

    exceeds

    s00

    mV;..

    eiagCr.

    _a

    ir,"

    o";..,

    *i,.."

    the

    bncrerial

    poputation

    in

    solulion

    exceeds

    ro,

    *rr,lir_.-rr,.

    pi,i-"[,.r,

    "i_*

    hat

    the

    firee phenomena

    prog.ess

    rhrough

    the

    cotum""

    ",

    *.r.,,.1.",

    ;;;;;;.

    4.f,.

    Discussion

    of

    Standard

    Expriments

    Appro\imrret)

    t5

    r0

    .

    ol

    rhe

    (opper

    r

    rh.

    m.,reriJt

    re|ofl,

    a.

    rcrJ \ot

    ble

    br,,chrnrire

    I

    pon

    agrlonrrdrion

    "ui,

    ".,a,t,,

    r,

    rrpr.ltr

    di,,oJred

    r,.,r...,,,.

    olurron

    or

    rhe

    d,, romerdre

    m ,erill

    o, r-.,

    *"o,rr',"i,r,i.

    ,.,p;;;,;i;,.i

    *"'

    (6)

    CurSOr(OHL

    +3H,SO]

    +

    4cusor+6Hro

    Yll,li-"li.lI

    *o *l,n

    recJ .orurion.

    rhe

    a(,J

    .orubrr

    copFr

    r.

    .rnpr]

    flu.hed

    ,u,,,

    ,ne

    corunn

    dr

    i

    rdre

    L.,nnr,,n,urJre

    $irh

    rhe

    rrnn,,io,

    ol.

    "na,orur

    or.,n^.

    :. :h{::rull.

    on,: rh. .orubre

    fopper,,

    ru,heo,,",,h.

    h.,i.

    "iii;;;,:;.,

    ,

    c

    rtd

    ontjnJle.

    lrorn,,\,JJlron

    ot

    thJJc,,crlr.

    ^:jl:::;:1:1"-"::l:nr(

    ilon

    reJchins

    ,,i

    (hJrco(

    ire

    p,occed,

    in

    rwn \rds(,

    rn

    ,

    r

    .,,iuJro

    cnrumn

    e\pe,rmenr\

    J rcni

    un

    proJu(ed

    by

    rhe

    bJ(reriJ

    r

    r;ri1

    v

    (

    {ured

    during

    firsr-stage.h:tlcocile

    leaching.

    rr,r.."J,u

    ;-s. i,rii'ir,li"i

    r..rr.

    i

    .

    n

    i,

    Lor.umed

    J.

    .o,,n

    :r, rt

    i, gencrJtcd

    A.

    a

    Jnn*qucr(e.

    ;

    ,.f..;;

    .;;

    ,'l

    ",.,"

    ,l'"

    ,orunon

    xnd

    rh(

    ,edo\

    pore,rr,at

    ,.",u,n,

    q,,i.

    r,,"

    "

    o,

    "."

    ,,,.

    ,(n

    t'.r..nlril

    ol .hrt.oL,te

    r:,pfro\imJrej)

    1/U

    mV r\

    Ag/ASCLa,;..;,;

    i;

    1.1,tr.

    ln,

    Ihr.et'te.ti.orrenmi,t,ten..inrrrJi.","rori^_,",,,"","i.^,;;,.'.

    rlrhough

    in

    ticl

    thc

    oppositc

    is

    true.

    .l'Ic

    rLrtr

    .l

    rvhich

    rtri.

    iron

    js

    ge

    crrtcd

    during

    this

    pcrio(t

    is

    govcmcd

    hy

    rhe

    ,rle

    nl

    whi(fi

    rhr hrctcria

    (

    oxidizc,i.irtrrs

    iRnr..I,his

    in

    1"",

    ir_inlf"c

    .(t;;

    "

    1n

    ,.

    trurrhcr

    (,1

    l

    .(tn\.

    n(lt:h

    l(rrrl)orlurc'

    nulticnl

    Ird

    suhslilrlc

    coDcerrlrxti(nrs'

    ,,.',,,u,ir',r.,r

    '+\|].',:'rrlt(,..,I,

    Lrrh('lrrhl'u't

    irlurnrr

    (\l\rtrrr''rr'

    rlr''

    r"lr

    rirn,,,,-'r,i.,,

    '

    ,'

    ir,.

    .','1r1

    ,

    '(rl

    r"

    rhc

    ttr(ri"n

    \rrJ\'

    AJr'{Jitrt'r"

    lqu

    rn'n

    (l)

    ir,"

    "-;'a"i,.

    ,,r r"*""r',i,

    le'ric

    iron

    requitcs

    acid'

    However'

    bec'luse

    the

    first

    slage

    ,,i'cIra;;.i.

    i;.g

    p-duces

    no elementar

    sulfur.

    and

    because

    pvrite

    leaching

    is

    ,

    "r,ii""J

    .,

    .,.

    r, lo$

    ;olu'ion

    purenrial'

    rhe onl)

    $ur'e

    or

    acid

    dunns

    rhr"rdse

    i.

    Ihe le

    d.olurron.

    Thu'.

    bdcre'ra

    \'tnrrnu'

    ro

    "\idr/P

    lerr"u'

    lo

    lenrc

    rron

    onl\

    ;";ii',il

    ,,,

    ,',,

    ol

    acrd.

    dnd rhs

    re'ulrs

    in

    rhe

    rir.r

    nage

    "r

    chrl'ocrre

    leJ\hing

    ;;;,;"i,"

    i; ,

    """."

    bJntl

    be)ond

    qhrch

    Ihe

    'olurton

    conEin'

    \itrudll)

    no

    irid'

    I"i"l,.^|.i.^*

    ,r,.

    *r,mn

    or

    iigtr

    pH

    ro""ntrrmed

    b)

    rhe

    dara

    in l-rgure'la)'

    ---i"

    ,i.

    *"r"

    "r

    ,t'"

    ii."t

    srage

    Jaliocire

    leaching

    fiont'

    leaching

    of

    the.second

    ',;"

    '.;'.ii;i.

    ,na

    ptnre..irrn'e'

    since

    borh

    or

    rhe'e

    reirrion'

    are

    rerdrrrer)

    .i"""

    "

    ".0r.",

    *,"p.tr,rres

    lhe

    rale

    ol lemc

    cun'umplron

    i' now

    mu'

    h lo$er'

    .n'l

    ii.

    ,"r,ui""

    pr*,lir.ri-ts

    to

    higher

    levels

    (600 1l)

    700

    mv

    rs

    Ag/Ascl)

    here

    i*iJ"r

    "-1j"i"".

    **

    rimited

    btlow

    fenous

    concentralions'

    can

    meet

    fie

    reduced

    i..""J

    r-

    r""r.

    non.

    This

    explains

    the

    relativelv

    rapid

    increase

    in

    potential as

    "i.*'Ji,

    tt..-p.r-"nts.

    The

    reaction

    proceeds

    more

    or less

    homogeneouslv

    ."".-,t"

    ".i."

    nrt,f,

    "f,ne

    column.

    md

    during

    second-stage

    chalcocite

    leaching

    il

    ";;;,ii;'"

    of-copper

    exrraction

    is

    soverned

    bv

    mineral

    kinetics

    ralher

    than

    rerpent limrrari,,ns.

    -?'gr'.

    ilro'.",..

    J

    'lishr

    ''lump

    in rhe

    cu

    lerch

    (une

    ror

    rhe tall

    column

    "'n"i,menr

    ,rround

    dav

    J0

    Thi'

    phen"men"n

    can

    be

    e\pllined

    wirh

    lhe [iFr-

    'r"i*.'rt"r"*1"

    lercrr

    ironr

    etfect

    Erpe"menr'l

    eviJence

    'uggen'

    rhar

    l-ir'r-srrge

    .ii.,","

    r",.r,i"c

    *.*'

    o'e,

    no

    mor"

    rhan

    rhe

    lenslh

    "l

    ru"

    'olumn'

    rno

    cm)

    ,,,,"'

    "".,i..,ii*rr.

    t).

    ln

    rhe

    o

    m co'umn

    rhr'

    uould

    a'counr

    ror

    onlv

    z

    'mJll

    ",',,,i"

    li in"

    s.a'm,',

    arrer

    dcrd

    rrn'rns

    onlv

    the

    lop

    laler

    ''

    acrtve

    iniridll)'

    *t"."u.

    rtre

    Ie't

    ot

    rhe

    \olumn

    i' idle

    lor

    ldck

    ol

    Jcrtl'

    Consequ'nrly

    rhe

    o\emll

    .." .i

    "."""i.,

    f*rr,i,e

    to

    the

    whole

    column

    charge)

    becomes

    verv

    small'

    As

    ,fr"

    J"f*.i

    "

    front

    moves

    further

    down.

    'covellire'

    and

    pyrite

    are

    lerchin

    in

    i;;;k;.

    ; as

    this

    zone

    increases

    in size.

    so

    does

    the overall

    potion of

    the

    ;;.;;.;,;it

    reachrns.

    the

    overrrr

    rare

    ote\rrdcriun

    rhus

    rnctea'e'

    rurther'

    once

    ;;;'.i;.",1.

    rronr

    ireur'.

    rrrrouerr.

    rhe enrire

    heap

    r'

    in

    r'

    ond''raPe

    reahns

    ^ri

    ii. *-"I

    rate

    of

    copper

    extraction

    corresponds

    ro

    that

    of

    the 'coveilite'

    '"

    ""l,ir

    zs,.

    *".".r

    copper

    errrrcrion

    stJdurllv de'line'

    rFrPUre

    2r'

    Thr'

    i'

    *en

    r'

    . ropologn

    al eriecr.

    u

    here lhe

    e\p'Fed

    'urldce

    area

    ul

    lhe

    copFr

    nuneral'

    ;;il.d;

    rvil,

    ti.".

    e.t.o,

    the

    leaching

    of

    mineral

    grains

    embedded

    within

    ;."

    ;;il.b'

    may

    be

    limiied

    bv

    the

    diffusion

    of

    reagents

    and reaction

    products

    ,r,-,i*r,

    *."*

    r].*"

    *a

    cracks,

    or

    prvented

    altosether

    bv

    occlusion

    (explaining

    -r,"

    io

    more

    ttan

    S:c"

    of

    copper

    has

    ever

    been

    extracted

    from

    anv

    colomn)

    Fe

    i,,i'""

    ",1""".',,,'"""ircriiir.

    on

    rhe"rher

    hund'

    d"conunue

    rn

    rlle\penminrs

    ii,.'',.",

    i.

    i ri''

    I.

    *

    r,'4,.

    "ru'n

    ir,.,r

    r'r.,',rid,r,or''crrtir)r"hirrrnPro$rrd'p)rire

    i.,ir'"t""t'"lrr(r't'+'(\'tn'h''hl)'h'1"'tr{JrrnrNrrlrirnl^ti(nhironlromrhc

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    soll

    es

    is

    subsr[nirllv

    (liNi

    ishcd'

    t0

    12

    il

  • 8/10/2019 Donat - leaching.pdf

    8/18

    l0i,

    4.4-

    tIllltsl,N

    ANt)

    t)tx()N

    Chalcocitc

    Lcaching

    Undcr

    COr-Limirins

    Conditions

    (

    llAl(

    rx

    lllr lll

    Al'lil()l

    I

    (

    lllN(i

    .t0 /

    1n

    lir.

    how.v.r.

    llt(

    (

    ()

    cotrlcrrl

    is

    only

    trhoul

    O.lT{'

    ol ll)xl

    ('l

    ()'

    (15{)

    fl)Dr

    (

    ()'

    vs.2l'1,

    o,l.

    llr[s,

    il

    ll

    CO]

    treeds

    ro bc

    ir(lv)rb.d

    lnnn

    lhe irir.

    rhc

    trir

    sulPlv

    nrte

    needs

    t(,

    b considerahly

    lister tlran

    what

    is

    requncd

    to

    srtisly

    thc

    oxygc'r

    {tcmnod

    fbr the

    same

    applicattun.

    Contnt

    iog to

    xbove

    cal'nlrtion

    on tlris

    hlsis

    Nsuming an

    average

    carbon

    yield o10.035

    mol C/mol

    Or and

    allowing

    ld cornllcrc

    CO,

    uriization

    -

    would

    requnc

    a minimum

    air

    supplv ralc

    of 0933

    Nnr'/nrr/lr

    or;bout

    4.5

    limes

    the

    rate estimaled

    for

    the

    necessary

    oxvgen

    supplv

    Hencc

    ir

    is

    reasonable

    1()

    suspecl

    that in

    heap

    leach

    applications

    with

    I

    low

    aerrlioo

    rulcs

    the supply

    of COr

    may

    in

    fact be overau

    rale

    limiting

    if

    there

    'ue no

    carbon:rlcs

    This

    is suppoded

    funher

    by the

    results

    of

    an

    experiment

    in

    a

    second

    6

    Dr

    hll

    columD

    on ihe

    orc

    material

    used

    in

    this studv.

    The second

    column

    was

    run ur)(lcr

    identical

    conditions

    to

    the one

    described

    above,

    except

    thai

    the aerxtion

    rarc wr\

    0.25

    Nmr/mr,ftr

    (without

    any

    enrichment

    with

    cor

    corresponding

    lo

    whnr

    is

    sed at

    the industrial

    site. and

    what,

    xccording

    to

    above

    calculation'

    would

    h(

    sufiicient

    for

    oxygen

    supply).

    Rsults

    from

    the

    leaching

    experiments

    are

    shown

    in

    Figure

    6.

    As FiguLe

    6

    indicarcs,

    copper

    exlraction

    fiom

    bolh

    columns

    proceeds at

    D(trc

    or

    less

    the

    irlentical

    pace

    until

    about

    day

    35 when

    thev

    begin

    to divcrge'

    ln

    th'

    column

    run under

    standait

    condilions

    this

    coincides

    with the

    day

    when thc

    polcnli'l

    rapidly

    rises

    ard

    noticeable

    quanlilies of micro-organisms

    are

    found

    in

    thc

    elllucDr'

    As

    discussed

    above.

    this

    is

    indicative

    of

    the

    narrow,

    acid-limited

    chalcocirc

    lionl'

    which

    is

    travelirg

    through

    the

    column,

    breaking

    through'

    However'

    neithcr

    ol lhcs'

    effects

    is obseNed

    in the

    columr

    run on

    low aeration'

    Microbi'tl

    bre'rklhrouglt

    occurs

    m ch

    later

    (around

    day

    60) and

    the

    potential

    in the

    cftluent

    ncver rises

    rho (

    500

    mV

    throughout

    lhe

    experiment.

    Although

    copper exlractior

    follows

    siDril

    r

    trends to

    those

    of

    the

    standard

    expe

    ment.

    it

    continues

    to

    lag behind

    by ahoul

    0l

    20

    days.

    This

    column

    also

    produced a

    consistently

    lower effluent

    pH.

    and

    Fc

    l' cl\

    in

    the

    effluent

    were

    consistently

    below

    the

    2

    g/l- in

    the feed'

    The discrepancy

    between

    the

    cxperiments

    is explained

    as

    followc

    Thc lirsl

    lo'l

    of

    copper

    extraction

    resulled

    from

    flushing

    ol acid-soluble

    copper

    rnd

    wtrs

    nor

    atfectid

    by

    aeration

    rare

    orCOr.

    This is fouowed

    bv

    the stage

    I

    phase

    durnrg

    whi'lr

    leaching

    ofchalcocite

    olcurs

    in

    a

    rel ivelv

    narrow band

    and

    is

    governed

    friDcil)trllv

    by

    the

    iate

    of

    acitl supply-

    Howevcr.

    in lhe

    low

    aeration

    column

    Cor

    suPPlv

    is

    piobably

    not

    sufficicnt

    to sust

    in the

    growlh

    necessarv

    io consumc

    all

    rviil

    blc

    ;cid.

    as eftluenr

    pH

    in

    this

    column

    st.tvs

    low.

    The band

    would

    thus

    be

    narowcr

    rn(l

    lravel

    at

    r

    slower

    prce,

    c(,nmensurutc

    wilh

    CO:

    rvtrilabilitv.

    as

    is

    wiltrcsscd

    bv lhc

    delayed

    brcakthrough

    of

    tnicro-organisns

    in

    lhc

    cftlucDr'

    Mie()bi'l

    sn'wlh

    itr llr(

    wrke

    of

    thc l'ront

    will

    be

    trtlc.lcd

    even

    more

    hy

    n

    hclt

    o{ CO' trs

    lhis

    ronc

    gr)$s

    l(,ogcr.

    tlclcc

    coppcr

    froduclion

    l.lls

    bchind

    iD thc

    low ticrrii(nr

    colunnr

    whik

    thc.tag.'

    I

    zorrc

    is sl,wly

    l,rlclirU

    lh(trrgh lhc

    coltrrno

    (hcc

    lhis

    hrcrks lhRnr|h

    (rrou

    (l(hy

    6{)) lhc

    rrlc

    (,1

    co|Pcr

    lc

    .hiDg

    hce(nncs

    sirnihr

    rgrirr

    in holl

    (rnIn'ns

    (ls

    in(l(irlNl

    hy lh(

    \lo|cs

    irr

    lrifu .

    {rr).

    in(li(

    lin8

    ll.t lI(

    rrl'

    rn \lUc I lcr(hin1f

    ir

    ()v(rirll

    ril.

    (l(l( rrrinirr

    llk

    r^irlili(nr

    I'l pliilc

    rrr(l

    {rllrrr

    r'rrrrirs rll"l(11

    A\

    $

    d\

    ourtinerl

    abore.

    (h t.ocire

    hrJp

    bioter.hrng

    u.ua

    y

    ernptuy\

    turccJ

    irruriurr

    sirh

    derauon

    rdre.

    in

    rndusrriat

    heap.

    rJnring

    r.om

    O.rjS

    ro,:

    n

    ,;:;;;.1;.

    ollo$inB

    catcutirion

    demon,rrare\

    rirur

    rhi,

    uoutd

    be,uificienr

    ro,,nol,

    :

    ;.

    \ygcn

    nceded

    for

    rhe

    conver.ion,

    rypi(Jlt)

    achreved

    in

    chslcocne

    hej.,.,

    A\sume

    a

    chrtcoc

    e

    ore,

    onrrrning

    0.8q

    Cu

    z.

    (

    u-S

    ind

    1%

    I

    eS

    lheore,.

    heap.bioreached

    in

    d r0

    m

    he"p

    "ris00

    kgrn

    *.i.j;;,t,r.

    ,,o

    :

    iil:i.;

    o achieve

    80"/o

    Cu exraction after

    t2

    montts.

    rrle

    pyrlr"

    .;;,;;;;;;;;

    time

    is

    esrimared

    at

    20qd.

    The

    fottowing

    overall

    reaOons

    apply,

    .

    (7a)

    CurS

    +4Fer+

    +

    2cur++4Fer++ao

    (7b)

    FeSr

    +

    l4Fer+

    +

    SHrO

    +

    lsFer++2soi

    +l6H+

    It

    is

    funher

    assumed

    rhar

    a

    Fer+

    is

    generared

    by

    bio_oxidation

    according

    ro

    (7.)

    4Fe2

    |

    +

    o.

    1411+

    *

    4p.]+

    n

    2,r,

    u

    Grven

    .rhe

    teed

    grJde\.

    rhe

    in

    iJt

    chat..ocrre

    toncenrrdrrorr

    rmouflrj

    ro 0.061

    mol4g

    and

    rhe

    plnte

    concenrrarion

    to

    u.JJ

    moy(g.

    olcr

    one

    vear

    the

    larseted

    convenion

    rare

    woutd

    come

    ,.

    u0.o;;;;;,;;,'.#i:,i.:;

    and

    0.0667

    mol*s/a

    for

    pyrite.

    The

    rohl

    {remand

    for

    .",f;;;;-;;;

    :::1:^:_'I :f^:1'*r-s

    (7a)

    and

    (7b)

    is

    rhen

    I

    r35

    ."r

    F",.;;;;

    ;;;;

    quatron

    (7c).

    0.284

    mol

    O.^e/,

    il l1"".ll_"1i",fr.,.r,

    "nj

    pai*,ng

    aen.iry.

    ar rorar

    or

    r5.000

    ks

    o,e

    wourd

    be

    pra(eo

    per

    m

    ur

    heup

    irea,

    lnd

    henLe a ror3t

    t

    "q";.a

    A, i,;;;;g.,;ffi

    i:il::ilif,:1"::1,,1,,"1

    i;'jl#'"Jff

    rareot

    Jbour

    450

    Nm

    /m

    /d,,r0.05

    Nm

    /rn)h.

    n,,lrng

    rhfl

    .n,,rmrl

    cundir.n.

    a.

    indi..areJ

    b)

    fie

    cdpldt

    lr

    ror

    ga,e.

    ,.r..

    ro

    itC,na

    I

    ",,

    ;;;

    1i:::11:l

    :".':''

    lhti

    zs+.oxfgen

    ''

    ,'',

    i;,;';;.'

    ';

    ;;i.t;',:

    i,i:;nor;*

    mJrErn,,r

    crrery.

    rhi\

    uourir,ussen

    an

    aerarr,,n

    rrre

    nr

    o.2

    his

    cafcufation

    would

    stipulare

    that

    aeration

    industriar

    operational

    praclice

    suffices

    ro..*.

    ut*t

    lower

    erd

    of

    lhe

    range

    of

    h""p

    H.**.,,

    ;;;;;;;;

    il

    ffi;;":iJi-}

    ::,,,,,i:JH,?.,J.T*i1f

    :"J:

    upply.

    Autorrophic

    bacteria

    common

    ro

    bioleaching

    "ly

    *

    CO.

    ;"

    il;;;

    .rbon

    source

    ror growrb.

    rhis

    is

    either

    &awn

    froln

    ;.b;*"

    .t;;;ls

    il;";.:

    ::l Ti'".1"1'.1r,.f.d

    rrum

    rhe

    ,urroundins

    ,".

    tu*,i.

    ",,Ii.,

    ,,r

    .,.;:,;;:;

    l;:l::1.11::

    g-,i"*"

    b\

    r4|o\riithn

    and

    A.idithnbd,ilt

    ,.e",.,.,

    ,.r,,,;i.,l

    ;;

    r rrerJlure

    rndrare

    r

    cdrbon

    )ietd

    oiUo,.2

    ro

    ni

    rnol

    C/rn,,io_,n,,i,

    t,,,,,,.

    \un

    Sche,pen/eei.

    Iqo6l

    BrecJ

    ,r d/.

    to,,,):

    Br,.e,t

    & xn\t,,r,t.

    Iu,,r/.

    .{

    ;r

    ;,rjr.r

    wo'ds.

    thc:rnrounl

    ot

    C(),

    Dccd..t

    is

    rbour:.2

    ()

    5Z

    ,,f

    ,f,".***

    ,,r:ii,

    ,",1,,;,.:A

  • 8/10/2019 Donat - leaching.pdf

    9/18

    llrlN(

    ll

    lrs

    (,lr(ll^l(

    (x

    llr

    llrr\l'lr(r.rA(llIN(i

    10,)

    ,,,"

    *

    "i,-

    ro,,r

    .,,

    F(

    /f

    Sck.kd

    to{h\oliheCo

    J,mired

    rdulllumn

    h

    ,

    ,

    ,,,,obiJr

    ,oun,

    , , ,.r",,,

    ".

    H,p"

    ".,.,,.,;,.

    "-,,:l

    ; .:

    ll-

    "if.,".,^,,

    "

    h,

    ..rtr,n

    tr

    n,.tsn,,Jr.

    aem,,on

    rchh,oo2s

    Nhih

    4

    .:

    il;

    ;;it;;,i;l'h,

    i

    r J,

    4

    -,h,J,i,,

    o'..r

    itr

    lhc

    [,w

    rcr ri,)r rolunrll as l(cslcd k, hy lhc

    highcr

    tll

    (i.c

    less

    oxidali(nr

    ol'clonrcnllll

    or

    fyritic

    sultu, rnd

    ihc k,wcr iron

    lcvels

    ir rhe

    ellluent

    (iar)site

    precipit.rtn)n

    nrste

    d

    of

    surplus iron

    generation

    tiom

    py

    lc

    oxidntion).

    Threfore

    it is

    possible

    that the

    lack

    of CO:

    afiecls

    primarily

    rhc

    rapid

    hn

    oxidalion

    of nage

    I chalccite leaching

    when bio-oxidalion can bccomc

    tutc-

    limiting.

    The slower oxidation of

    second

    stage chalcocite

    remains controlle.l

    by its

    slow m ineral

    oxidation kinelics. Unfortunately theexpenmeni

    is not

    tully

    cooclusivc

    in

    this

    regard,

    since the rate

    of

    air suppty

    ;n the low

    aeration

    column was also

    close

    to that

    required

    for

    oxygen demand

    at

    the

    given

    rate

    of

    leaching

    (but

    w.rs

    not

    limiting

    as il would

    have

    been

    for COz

    demard). Nonetheless.

    the study

    crD

    be taken

    as

    an indicalor

    thal

    low

    aeration

    rates

    practiced

    in

    some heap

    opcrrln)ns

    may

    be limiting the

    overall

    rate

    of

    leaching

    more

    than

    necessary

    and should

    hc

    4.5.

    Chalcorir Laching In

    High Salinity Process

    Solution

    All

    standard column experimenis

    were

    run

    with a microbial culture

    grown

    in

    the laboratory under

    optimal

    Srowrh

    conditio.s

    before

    introducing these inlo thc

    columns,

    and

    the feed

    solution

    contained

    only

    rcid

    and iron.

    In

    real

    heap operaiions.

    however,

    conditions

    are

    generally quite

    far

    removed

    from

    such an

    ideal

    situatio[.

    and thus

    microbial

    suryival

    and

    efiiciency

    are more seriously

    challenged

    (carcir

    "1dr.

    1998).

    Feed and effluent soluiion

    (raffina.e

    and PI-S)

    samples

    were obtained

    from

    lhc

    industrial

    site

    fiom which lhe

    ore

    material

    had

    been

    sourced.

    Microbial aclivily

    was low in rhe

    PLS

    and viriually

    nil

    in

    the

    raffinate.

    The

    chemial composirn,r

    of

    the

    raffinate

    (which

    is

    the same

    as

    the PLS

    except

    that most oI the

    coppcr

    has been

    removed)

    is given

    in Table 2.

    The

    concentrations

    of

    dissolved

    salts

    [c

    exceptionally

    high, with magnesium

    and aiuminium alone

    accounting

    for

    aboul

    959.

    of the lotal

    dissolved

    salts

    (TDS)

    at

    148

    g/L.

    Such

    concenlralions far

    excecd

    7,r/. 2. Anlly7ed

    conrposllion ofthe ralfimtc ar rhe indunnal olnrn)n (only

    componenh

    >10 m /1,

    Elemenr

    Concentrarion

    t.dl-l

    Mg

    K

    l:.100

    lt6

    2]l

    CI

    I

    231

    tll

    )l(r

  • 8/10/2019 Donat - leaching.pdf

    10/18

    I'l

    t{sr

    N l\Nt)

    tn\0N

    k,lcrrncc

    lcvcls

    klDrlc(t

    ir)

    lhc

    Iilcr

    urc

    ti)r

    i|1nr

    (,xi(tj1iIA

    lrk.r()

    itr

    rrinra:

    l]tirl,r

    andRrrllh

    (2{)0.1)

    indicrrc

    a i,nDedi,r.

    tive

    lbrd

    dcct,,"

    ;

    *;,*,;1,,i;;;,

    ,;;;,

    ;l;_

    N.rrSOr

    soturion.

    tnd.

    nr

    an

    exrension

    ofthis

    sludy,

    Srri",.

    ")1.

    lZxrS;,"1r,",,

    ir.

    e.manenr

    retardation

    of

    growrh

    rate

    ar

    lhis

    concentration

    .t ru",Sit..,

    r,)u";,,.,

    er

    dl

    (1971)

    repori

    an

    adveBe

    effect

    of Al

    concenlrarions

    exceeding

    r,i

    glr_

    ",

    ir,"

    growih

    of

    ar unspecified

    (A.idi.)thiobacillus

    srrarl..

    ,

    Furihermore,

    the

    chtoride

    concentration

    of

    L3 g,4_

    is

    aiso

    of

    some

    conccm.

    Lawson

    e.

    dl

    (1995)

    report

    on

    adverse

    erTects

    on

    microbiat

    growrh

    of

    chloride

    troncenrarions

    e\ceedrng

    I g/L

    $

    rth

    comptetc

    rnhihiuon

    ,

    Z

    "rf

    .

    Sf,i.^

    "

    rliinni,

    ::Y

    l'll1l

    1":'*1."

    ,r

    gr,,s

    rh

    rsre

    r

    ts/L

    and

    r

    c/L

    \Jcr.

    bur

    ",rr,

    ro,e

    r..;

    trerery

    rnruugh

    dJ

    prarion.

    Jnd

    permdnenr

    rerardatiun

    ar

    higher

    concenrrartn,.

    rne

    nrdh

    Larron

    concenlration\

    re,utl

    fium

    rhe

    errduzl

    Jj*otution

    ol ,iti(ate

    ii:r:^: lil.lll

    rin

    rhe

    prc.enr

    ra,e prima,ry

    chr,rrrre.

    biorire

    ,,d

    pr,g,,;i;;;

    LdmDerg.

    tee/

    r

    dId

    the

    tacr

    lhdt

    lhe enlrre

    \ntulion

    iru.nrory

    i,.onr,nroriy

    r..i.-

    culated,

    wilh

    onty

    copper

    removed

    in solvent

    exrrac,;.,

    _a ,"

    p*g..

    ffr".,frf_ia"

    concenrration

    relates

    primarity

    ..

    the

    dissoturion

    of

    ",,"".t,"

    iC,Arc,ii;;i,i

    chloride-conraining

    copper

    oxide

    minerar

    which

    **."

    i,

    tl,"

    ,* ;i,

    i.#

    A

    mrLrubidl

    culrure

    ur\

    erJdua

    )

    enrnhed

    ind

    mdinrarned

    in

    rh...i.,i-,r

    u,,ditured

    rJriin,e

    ,n

    I

    \h.rter-incubrrlr

    ar

    rs0

    rpm

    ar

    i0";.';;;.

    _;,

    i;:

    ;l:.':

    inoculare

    a

    4,cotumn

    experimenr

    which

    was

    run

    with

    th.

    .,ffira..

    ,.

    f".,t

    ,;;ii";:

    but underotherwise

    idenricat

    conditions

    to ihe

    standr.,t

    ._p"rt."r,.

    ..;"rJ;;;;.

    The

    r.ulr,

    tr,,m

    rhe

    rw,, 4-c,,tumn

    exleflmenr,

    rre

    ,

    omtred

    in

    Figure

    /

    .

    rrBure

    ,a

    \how:

    lhe

    copper

    e\lraction

    r,.

    rrne.

    tn

    b,,rh

    erperiinenr.

    rhe

    trrrr

    lU'.

    or

    copper

    exrructiol.

    retre\entrng

    ,he

    rin\ing

    o,

    *U

    *frf,f.

    ,

    "pp"r.

    ,. ,"pi,jfi

    nu.hed

    lrom

    rhe

    (olumns.

    Orer

    rhe

    nexr

    looa

    ol

    c,,pper

    errrdcrn,n.

    ,irgr,r,

    ."..*

    ,prnding

    lo,tcg(

    I

    ierchrnts.

    lh(

    t$o

    e\prrimenl.

    ditler,ipniticrr,ly:

    t" r;".H;d;;

    e\Penmenr

    rhr\

    pha\e

    i.

    neirjy

    comptete

    with,n

    25

    dr)..

    "t.".",,f,..rp.ri..r,

    rlh

    n

    rve cutture

    dnd

    rdlfinare

    \oJIrron

    requirc\..t0

    J,ry,.

    Leachrnp

    rren,ti. rre,..,r

    n0%

    clrac,ion

    rre. hosever.

    rerl

    ,imir.rr

    in

    borh

    er;;;;:.

    '"

    "''*'-*,-

    ,":,,r",:; il

    "il

    l: lT-

    rh.

    prosre*;on

    ,,r

    pH

    anj

    .orurion

    po,cnriar\

    ajons

    rhe

    '(

    arIr

    or

    Ine

    \ePmenled

    column\

    Ihe

    cur\e,

    ret

    ing

    ro

    rhe

    \rdnddrd.t-cotumn

    :.l:.iln:no

    ,h"y

    Gimirar

    ro

    Figure

    4a)

    chalcocire

    (low

    potenriarl

    i"".r*g-i,

    "

    anow

    zone

    movins

    down

    rhe

    column.

    folrowed

    by r,igr,

    poiemior

    ,rug.

    z

    r#r,;ngl

    In

    lhe rallinatc

    expcrimenl the

    {age

    I

    zone

    rs,ritj

    obsenrd.

    br,.i,

    p.";;;:,.,

    much

    more ,towty.

    dnJ

    lhe

    rran,ilion

    irom va:e

    r ro

    ,rage

    :

    fe,,

    hrng i,

    m,j

    .or.,

    gradual.

    Only

    some

    of

    rhe

    available

    acid

    js

    insumed,

    and

    the

    pH

    remains

    more

    or

    Ie*

    nrble

    $irtr

    ont)

    tr

    mrn^r

    pe,,[

    aruund

    day

    )U. $hen

    lhi f""

    p.,",,,,"f

    ,.ri

    fliil'

    ,l.".lgn

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    I

    i,

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    rhfl

    .,rse

    I reach,ns

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    ,hrousi,

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    ,,,ri,","

    corumn

    wrthrn

    r broad

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    rrrher

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    d

    nan

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    'uppt1

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    opp".e,t

    r;;il:;;il;.il;:;:L

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    anJ

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    n"r

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    \.

    pt,,fi

    ,

    rl(.

    rumber

    ofbacEria

    counted

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    sohtion

    as

    I

    function

    .f,i..

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    shows

    counts

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    ilude

    iD

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    r,*:r",i,,

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    Z

    Sulccted rcnr16

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    dr.4 colu'nn

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    under

    (rnd{d

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    ir6n:

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    i) tr) com$cxtncrn)n:

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    pr) r.*n,r

    ol n'luron

    por.trrrl

    in iodrndll rrl,in.te

    rs

    crnnpared k)

    the

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    (nl

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    Ncve(hclcss.

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    wilh

    nnrnhcrs nr)vin8

    down lhc

    colurntrs in.

    tr)wi[g

    wlvc . llc

    pr('pxrrli(nr

    rntc,,1

    llis wrv..oircsponds

    to

    llxt

    ()l

    th( hi8h

    l)oicnliirl

    wrvr i tlc wrkc ol

  • 8/10/2019 Donat - leaching.pdf

    11/18

    }l

    t,t

    :RSt

    N

    ANl,

    t)t\()N

    |lllNr

    1l1l

    s

    ()l

    (ll,\lrrI

    lll

    lllAl

    lrlr)ll]\(lllN(]

    s

    E

    l.mE+o?

    3

    t 00E+06

    E

    I

    nut*05

    Fis,/.

    &

    Bact rilt

    counr

    oler

    the

    lengrh

    oi rhe

    cotunn

    i. experiDenrs

    25

    and 28

    Iarlc

    J.

    Crowrh

    rate

    and final yield

    or

    srcwrh

    experimenrs

    tr.((,1r,,'\.irr'{r\

    ll'rrl'5rrrr

    'r

    "'rrrtrrlt'rr'r\r

    rrrtrlr'hrrr'rrr''l

    'l'\rl"l'11

    h\ rlI

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    .\

    l,,v{,

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    ''

    '.rl"

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    LrIl'l')'11

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    xrr rrl ccliur

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    nxxl0l

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    lirr

    rrntrsl)orl

    ('l

    ",rr".

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    L"q,,trxl

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    rrtircrdl

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    rhc

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    ruhi

    rcllcri('rr

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    ;,h.

    ;i"Jl

    sirc

    i,rco,'r,rtrrirg

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    microbitrl

    stouh

    nd

    orid'lrnrrr'

    "rJ.i,,"."ir"""r,;rg

    ,r,'"nsh

    app;prirle

    kincdc

    rcms

    Additn

    rl

    ttLiturcs

    includc

    an

    indeDrnderrl

    heulh(rl

    hrhnJ

    xnd

    J

    gJ' Ina"brlur'('

    -

    i*"',^*.',,il.."del

    are

    t'l

    prrrrculJr intetr'\r

    rrr

    lhe

    (i'nr(ir.l

    rh

    Pr(r\'rr

    ar..,*,.":

    rr,.

    fir't,rldre'

    Io the

    $r) rn

    $hith

    hull

    \rlurrun llow

    i' rn'{l(l\l

    iil'ls."In.J

    it'"

    *ut.n

    flows

    throush discrete

    channels

    in the

    ore

    bed

    which

    ,."-i.

    .""i*r

    \vi

    rt

    "

    a"ster

    of ore

    material

    containing

    an

    aqucous

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    lhc

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    moisture.

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    flow

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    the

    predominant

    mode

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    mass

    lranspotl

    rtr

    ,fr.".

    "r,"r,r'.f",

    *fr-*"

    *ithin

    the ore

    cluslers

    it

    is bv

    molecular

    diffusion

    lhroush

    ii"-",""",i

    ,or

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    ne

    drnution

    lens$

    Rri'e'

    Ihe

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    or

    lhe clu\r(

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    .i",".L','ir.

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    prrJmeter

    The

    larset

    rhe

    'lu'rer

    i''

    rh'

    lurrher

    rexg(nr'

    rhl

    .""",,-

    *"a*,'

    tt,ve

    ro

    artir'e

    lhrough

    \lagnr'nl

    'olulron'

    ln n

    rro$

    rulurnrh'

    'J

    r'

    ,1..a

    in thr'

    'rudv.

    R

    c.n be

    raken

    ro

    be

    clo\e

    ro

    lhe

    pipc radtut

    {8r)"

    "i

    ruai"'

    r1*

    been

    fo.rni

    to

    be a

    goo{t

    value'

    ie

    4 cm

    in

    the

    present case)

    lD

    un""nii*a

    r,*p"

    irrlgrr"d

    bv

    &ip

    emitten

    it

    is likelv

    b be

    much

    larger'

    ck)ser

    t(l

    tr'.-r,"ii

    iit"".'"

    t"*"*

    two

    drip

    poinls' This

    has

    been

    discussed

    in

    some

    derlil

    ,na oarrirllr

    conrirmed

    rhroutsh

    er|enmenls

    b)

    Perer\en

    and

    Di\on

    (2001)

    -

    -n;;i;;,

    "'p..,

    rerare'

    r"

    microurot

    o\idarron

    shrch I'

    rnodeleJ

    rhr"urr'

    lai.U.ri"l{*t*

    tin.ti"s.

    combining

    micrcbial

    growth

    with

    ferrous

    iron

    oxd

    rrnr

    ,;u tfr"

    pi.t

    "quutio,

    (p"t"rsen &

    Dixon

    20Mi

    Ojumu

    eldl

    '

    2006)'

    Thelbaudur

    '';.

    ":;.i.1

    in rhi'

    approdch

    is

    rhe

    ,primum

    microbiul

    srosrh

    rare

    (

    '

    r.rr(rr

    ''l"r

    refened

    ro d'

    1r,..

    ,

    \^hrch

    I' m"Jrtreil

    b)

    Monod

    and re\i\larrce

    rerm\

    ('r

    'tr('{urr

    t-,i"

    "ii""

    "r'iil'u",o.

    "oncentrarions.

    temperaturc,

    c'c'

    Tvpicxl

    values

    fi'

    t

    lin

    "

    tr.r'ltfry-rrt-"..y

    *r,rre

    and

    a

    native

    culiure

    stressed

    by

    high

    concenlratnnr\

    ol

    Mc rnd

    Al

    'ullJre'J'$ell

    a\chl

    rde\

    are

    reflecreJ

    inT

    ble l'

    '''ir,i.,r",

    'r,.

    .""a"a

    ,{olumn

    :rnd

    Irll column

    re\r'

    di'cu-etl

    dbn\(

    $cr'

    rr'('l

    .

    .urii*,"

    ,r',.

    U*pslln

    .odel.

    This

    is

    a

    some

    hat cumbeNome

    process

    describc(l

    i.

    In"*

    a""

    elsewhere

    (Dixon

    &

    Petersen.

    2004:

    Pete$en

    &

    Dixon

    20o6h)

    O.""

    "rriUt""a,

    ,h(}

    -.ael

    can

    then

    be used

    to

    simulate

    other

    column

    expcrinrcrtts

    Jrrriir.r,,*i*

    ,r,.

    *levanr

    operrrionrl

    pJrrmerer'

    r'uch J' rlos

    rr're'

    e"lrtttur

    i"iJii.

    iJ.a

    .","'r"-i,i-.

    ",.)

    b 't ieat ins lhe

    inrrinnc

    prrJmerer'

    de\

    ribrnr

    rn,rrrrl

    ,,i.i.-il,i

    r,""1.'

    ""d

    ma',

    r,on'rei

    p'r''m'rer'

    unchrnseJ

    ln

    rhi'

    r'r'hi"n

    rln

    4-cotumn

    experimenl

    has been

    simulated.

    as

    is sho$rn

    in

    lcrms

    of

    coppcr

    exlrrcl(n'

    '"i;"r..

    o.

    -a

    't.

    ,,,,,r,he

    Lxperimenraldrl

    r i'

    vet)

    8o"'l'

    Sirnili

    lv

    f''\l'inrrt}'

    rions-r.rnrtrchier

  • 8/10/2019 Donat - leaching.pdf

    12/18

    tinE

    on

    slream

    tdaisl

    ll r,?

    9.

    SiDrtlrions

    oI

    .1

    cotuDn.

    s-.oluro

    xnd

    hti

    cot,trnn:lrndurd

    erpernrenrr

    '

    r \r'

    '

    tr

    ll

    ]ll

    l\l'lrlo

    r1( rrrNri

    .7lr.rr,Iil)ttrr\t,itr|rr,

    ll'

    t(rr,,,r.,rrl

    sl,(\\.(l

    hr(l(rrr(/,. 0l).1 h

    )

    llrs

    eo,rcst)(nrlr

    lr'

    lltr ,trlu,rl

    ()ttr

    rrlrll

    L(relili(ns I

    llc

    rrrirr.

    sil..l lhc lirrr.,)l lltr'

    .

    70 cnr

    drippcr

    s|r.ins

    (/(

    =

    .10

    cnr)

    .nd

    ltrllhy brclcril

    ((

    =

    (l.l

    h

    ).

    .

    50

    cnr

    dritpcr slrcnrs

    (R

    =

    20

    crn)

    aDd

    suessed

    bacleria

    ((*

    =

    0.02

    h

    ).

    rr(l

    .

    50

    cnr

    drippcr

    spacing

    (R

    =

    20

    cm)

    and

    hcrlthy b.rctefitr

    (lL

    =

    ().1

    h

    ).

    H.re.

    nrcsscd bacteria

    referc

    to

    the

    combined eftects

    of

    high srliDity

    rDd

    txncrr

    rially

    limitcd

    CO: supply

    on

    mic.ohinl

    growth.

    These

    efiacts

    int

    at

    ptclcnl lor

    described

    tbc

    model

    explicitly. but accounlcd

    for

    ihrough

    a

    reduction

    ol

    thc

    laluc

    of the microbial

    growth

    constaot

    t".

    -or

    all

    simularions the

    heap

    was taken

    ar l0 m height,

    lhe lied

    rute

    at I0

    L/rDr/h.

    and the

    aeration

    rale

    at

    0.25

    mr/mr/h.

    Feed conposition

    included 2.0

    g/L

    ol

    ir(nr.

    Also,

    the model

    was

    adjusted

    to

    the

    geo-climatic condirions of

    the heap

    localnnr

    rn{l

    lemperature

    was

    left to

    self-adjust

    (as

    opposed

    to

    imposed isothermal

    coDdilnnrs

    when modeling column

    experiments).

    Modeling

    the

    hexp under aclual operating

    conditions

    (long

    drippet

    sp

    cing,

    stressed

    bacteria)

    predicis

    approximately

    757.

    copper

    extmction

    wilhin 400

    (lirys

    (13

    monihs), which coresponds

    well with

    reponed

    producft)n figures al thc

    linre

    (Garcia

    "/

    a1.. 1999).

    At the

    srmc

    time

    this

    is

    considerably

    longcr lhrn rrry

    (n

    tbe

    labomtory

    experiments

    rcporied above.

    The

    primary

    rcason is thal lhe h.gc

    stagnani

    clusters between

    solurhn

    channels

    enforce a long diffnsion

    prih

    1()l

    th(

    delivery

    of one

    key reagent

    the

    rcid needed

    for the

    bio oxidation

    teaclnn)

    (l).

    Petersen and

    Dixon

    (2003a) have

    shown thxt,

    as

    a

    consequence.

    tho

    zoDc

    $i c

    .halcociie

    leaching

    described nbove

    proceeds

    'sidewayi

    in he|ps.

    awry li,,r)l

    the

    solution

    channels into

    the stagnant

    cluslers.

    as opposed

    to

    dowDwnrd\

    rs

    irr

    tr. ,,r.

    7,

    Snnuhtu.

    of.1coltrm.

    N&dard

    md.l

    cotuD.

    rull,nare

    experimehrs

    insteJd

    ,,t

    2.U

    g/L

    rn

    rhc

    srlnd

    rd experjmenA

    I

    or

    rhe

    r,rrr

    col,per

    errncr,";-::;il ;;;";;tile

    2'

    rhc re'ur'

    ae.,,,

    in,e.r.

    dira.

    A8,,,.

    rhe

    ,noder

    r,,.

    rhe

    ..r";#:;.'

    I0'

    roserher

    $rrh

    rher\penmenrri

    cr'J,5 (ap,uk.

    ,r,e

    ,e,J,d',on

    ,;

    :;;:,1"'"

    uerr

    over

    In'^r

    ur

    rhc

    ru.

    nd

    Pe,

  • 8/10/2019 Donat - leaching.pdf

    13/18

    A\rl,(,,rt,rr

    \

    n,rtrrr,,,,\.tr,w,tt,,,r

    ,.,.

    ,,q,,

    .,

    r,,

    d,

    xc,r,",,

    .,,:l

    i.t"lii'l'

    "J;l:l:.il:

    :il,l:liilll,;:i]i}

    nJn(r.

    r\

    d,,e\

    rhe

    u{e

    or

    J

    heJllhv;r.

    rht'ruo.rlecr\

    .

    ,i,

    r.',,

    ,,,1,

    *"i',,i,,,,;

    '"li't

    e"r"'n"'e'r'

    rhi{

    inrhJr"'

    rh,,l

    -

    rre

    b,',h

    rure-r;mirins

    ;,

    ;,;:;i

    ;"#l'

    ::f

    ''i'

    and'erJrd(d

    mrcrobur

    p,,'wrh

    e'renr.

    Re,rucet

    an1pei.r,.,,;;;;;;1*'

    ernJcrron

    r.

    appro\imarerv

    rhe

    .JmF

    ,"

    n.,.".

    "".n,iJ.i",i;i'

    :il"

    il:H

    :T,l,li:,::ffi."1HJ":ilii,ff:

    As

    Fi8ure

    tj

    indicares.

    more

    sipnjfi.,

    micr,,biJr

    hedrrh

    ',,,,.

    r,.-

    *,,,i,?j'i-'"';'r

    improvement

    courd

    be

    m,,de

    if

    rhe

    or

    *ri"""'*-'r'i"li;l

    ;:il

    ;l;ilXi'"

    9'

    reducins

    rhe

    rever\

    or vts

    and

    pe,e^en

    h

    s \hoqn,hJ,

    s.,..;,;;;

    ;;;:I";l's':''rron

    t

    npubri\hed

    ,.u

    uoir

    r,u

    *,,,,cr

    ',,.',n,,,i.d

    ,"rii;;,.':'",',,",j;

    'i:

    'n:

    *)n.

    oreirhcr

    Msso,

    Ar

    rso

    )

    ,,e\

    o,

    ,hc

    n*,ve,,,,;;;;;;;:::.

    ill

    o"nl

    jna'

    imro\eJ

    microbirt

    groJrh

    h,,qcve,.

    rhr

    *h,.,,,c

    .*|;;;,.,;;,"1

    "

    '':':'oi

    2-3

    r,

    i'

    ,.rno$redse,r.

    1ay

    in

    racr

    be,

    nprrcrica,:,

    ;r;:,"il,::,,,,il1:i,:::J;:,::,;jI",;,;:l#

    rne

    rndDstrjat

    opemlon

    L,,rt,t

    U",lno,or"a,

    or in

    e\ce\.

    or

    su,

    j

    .^

    i,r,ir.r",",l'""

    "'t'chieve

    80'

    in

    a'

    hrrle

    J'

    250

    d:r)..

    6.

    CONCLUSIONS

    Herp

    biuje

    chinS

    ot chrjcoc;te

    ore\

    r\

    wide

    'sn,rrcJn,

    ,ndu,rndt

    a.pj;carion

    or

    oa".,.r'l

    t'":l':.0

    and

    rhu'

    bv

    lrr

    rhe

    mo\r

    p-..*

    ''

    q,;r.

    .o,prii.

    ;;1,,,;

    :;:

    "

    'e

    Arrhoush

    ir

    "ppea,'

    \imnre.

    ,hF

    ,rhro

    organ^m,.

    ctu.re^

    or

    pon,,

    t.,

    ur.t ,r,"

    ,t"t' 'l

    lhe

    'rale\

    ot

    mineral

    grarn..

    ""y,rrr,ia,"

    n,,r:,r*q,,r;.ii,;,;i;';;,X;;**,\

    auh,re.

    rhich

    can,n,e,J.,,n

    modcr,ns

    ,,,or.

    ',.h

    ;,

    il.:rit;.

    ;.

    i;;'""'on

    drone

    and

    requrre

    a

    comprehen'i,e

    ,n,enar

    hr'

    \houn,ha,

    u;;l

    ;

    .;,il:#

    lh'

    rorumn'ru'r)

    on,)pi.

    rr

    o,c

    he

    dchievabh

    ,,,,n1

    rr.,^

    "',rr,,

    "

    i.*

    r'"'rrlron'

    hiSh

    copper

    e\rrucrn,n5

    .hnurd

    rd,r

    ,har

    much

    r.."

    .,,,"",,,,,".,

    ,;:,ii'.,:l

    ,,

    amb,cnr

    remperarure.

    rhe

    d,lerm,qed

    b)

    ,""

    ,,i,

    ,,.,.^

    f;;,;

    ;J:"

    reJri')

    rn

    in'ru'rrrdr

    operar,,'n'

    i.

    u

    rrhin

    rhe

    herp

    due

    ro

    ro.";;;

    ;",,J;,'JT::ii

    tinrihurion

    re'pe(iJiv

    or

    J,

    'd)

    mL

    obJi

    .ri\,)

    o..

    -r,,,,'.,ir.'."r,,^fl..L-"iiii..iilL]:l,llll,,il.l?,"

    5uPpl)

    could

    al\o

    porenria

    y

    rerard mrcrobiz

    concru\rtetl

    denron\rri(eo

    '

    growrh' bur

    lhi'

    ha'

    n"l

    yet

    been

    L

    {

    nod(irng.

    nudy

    u.jng

    lhc

    Heapsim

    root

    hi.

    \hu$n

    thit

    lhe.e

    lw,,

    e|leil'

    Jve

    an

    overdtt

    r.l,e

    timilng

  • 8/10/2019 Donat - leaching.pdf

    14/18

    I

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    Microbial

    Processing

    of Metal

    Sulfides

    edited by

    Edgardo R. Donati

    Unhtersity

    of

    h

    Plata,

    Arqentino

    and.

    Wolfgang Sand

    Unbercity

    ol Duisburq-Essen,

    Cermany

    A

    Springer

  • 8/10/2019 Donat - leaching.pdf

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    A

    (

    I

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    I ih

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    ISBN

    978-r-,1020-5538 r

    (HB)

    ISBN

    978-l-.1020-5589 8

    (e

    btuk)

    Published

    by

    Springer.

    PO. Bo\

    17.3300

    AA

    Doidre.hr.

    The

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    2007

    spri.ger

    No

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    work

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    srored

    in

    I

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    q.rk

    TABLE OF

    CONTENTS

    l'rcfuce

    scclion

    I

    Fundamentals,

    microorganisms

    and mechanisms

    I Microorganisms

    involved in

    bioleaching

    and

    nucleic acid

    based

    molecular

    me.hods for their identitication and

    quantificatio,

    Arel

    Schippex

    2.

    Mechanisms and

    biochemical fundamentals

    of

    bacterial

    metal

    sulfide oxidation

    Thorc

    Roh||erder

    dnd

    wolfgang

    Sand

    l. Electrochemical

    techniques used

    to sludy bacterial-metal sulfides

    interactions

    in

    acidic environments

    D?nis. Retilaqua,

    Heloisd A. Acciori,

    Assis V. Benedetti

    a|d

    Oswaldo

    Cd":ix Jr

    .1.

    Catalytic role

    of

    silver

    and

    other ions

    on

    the

    mechanism

    ofchemical and

    biologicd

    leachiDg

    '77

    Anto

    h

    Ballester, Marid Luisa Bld.qut.,

    Felisa

    Co

    .tile.

    x

    .l

    Jesns

    A.

    Iluiio.

    5. Rccovcry

    of

    zinc. nickel.

    cobah and

    other

    metals by biolcnchirg

    103

    llurisd Vietu,

    Crinnu

    Pogliot.

    Elsd lo Do oti

    6.

    lliolcaching ol

    nrcl.lh in

    ncrtrrl Id

    slighlly

    rltrlitu

    ctrvironnrcnt lzl

    Al.kut

    dRt Sklt\h\*a t

    nl lttlru|n

    Mt htk\$kn

    t5

    5,]

    l\rrl rn

    r

    0Nll

    Nrs

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    S.( lrtir

    ll

    lli(r.itrl(nsrrkl llkn'er|\

    /. lli,,lc

    chirrg

    ()l

    sollidc

    rriDcrxls

    in

    .oDliDuous

    (iRd

    t.uls

    Lx)tittitttk lI(ttri

    Ro ('

    Mori

    l]r

    t:t:l

    193

    2t9

    221

    253

    265

    261

    )t\'7

    'lll

    8.

    Bi(rcactndcsigD fuldrnretrtals

    nd

    then application

    10

    gokl

    mining l5l

    Fer'ldndo At?wdo dn.l Judn

    Catk,s G.tlti

    a

    9. Airlift reactors: characterization and rpplications

    in

    biohydrometallurgy

    Alejondrd

    Gtuve o, lnurd lntdll,

    Patticia

    Chidcchiari

    i

    atd

    Edgatdo

    Do xti

    10.

    Principles.

    mechanisms

    and dynamics of chalcocile heap

    bioleaching

    Jochen Petetse

    0 d

    Doti4 G. Di\o

    Section lIl

    -

    Cenetics

    and Molecular Biology

    I

    l.

    The

    use

    of

    bioinformatics and

    genome

    biology to

    xdvance

    our

    under{:rnding ol

    h

    leJ(hinE mrcroorganism:

    Raquel

    Quatrin|

    Jorse

    Vdldes, EuRenia

    Je(llicki

    .t d

    D.t|i.l

    S.

    Holules

    12.

    Protcomics

    and

    metaproteomics

    applied to

    biomintug

    microorganisms

    Ca

    os A.

    Jerc.

    l3-

    Cell

    cell

    communication

    in

    bacleria: A

    r,m,,iritry

    net|

    aproach

    to

    inprcve

    bioleachinq

    ellicienq l

    Susa,la Wllet.uela, Alwto Ro

    deras,

    Carh^

    A.

    kre. .i|d Ni.okts

    Cuilia

    i

    Seclion

    IV

    Other Applications

    14.

    Biollolation

    nnd

    bioflocculrlion of relevoce

    to

    minerals

    bioprocessing

    K-

    HdnDM

    thn

    Rao

    u'td S.

    Sub,dnrntiot

    I5.

    Hydrcgcn

    snllidc

    rcnn)val liom grseous

    etfluents

    .lo /

    Mtit(lGtnN.

    ol l)tr i,tlo Cankkj

    t69

    241

    LIST

    OF CONTRIBUTORS

    ll(ft)isa

    A. Acciari

    Universidade

    Esradual

    paulisla,

    Insliruto

    de

    eunnictl.

    I).pfl1lrnento

    de

    Bioquimica e

    Tecnologir

    Quimica,

    AJaraquara,Sp,

    Brxzit.

    l,rDando

    Aceyedo

    School

    of Biochemical

    Engineering.

    ponlifical

    Cathotic

    I

    rniveftity

    of

    Valparaiso.

    Valparaiso.

    Chile.

    ,\ntonio

    Ballester Depanamenlo

    de Ciencia

    de

    Matedales

    e Inseniclir

    Mcralirgica,

    Facultad

    de Ciencias

    Quimicas,

    UDiversidad Complutense

    de

    Madri(I.

    \'hdrid.

    Spain.

    ,\ssis

    V. Benedetti

    Universidade

    Estaduai

    paulista,

    Instirulo

    de

    euimira.

    I

    ).plr,rmento

    de

    Fisico,Quimica, Araraquara-Sp, Brazit.

    Nlaria

    Luisa

    Bldzquez

    Deparramento

    de

    Ciencia

    de

    Mareriales

    e

    hgenicrir

    Nlclahrgica,

    Facultad de

    Ciencias

    Quimicas.

    Universidad

    Complutense

    de

    Mndri(t,

    i h.I

    id.

    Spain.

    r\lvnroDanderas

    Unit olBaclerial

    Cell Communicalion.

    Laboratorv

    ofMotecutxr

    \4i.

    r,'hrolop)

    and

    Brorechnol,,g).

    Depdnmenr

    ot Brotopy.

    Facutrj

    ui

    S.i

    ((,.

    lrriveNity

    of

    Chile, Santiago,

    Chile.

    I)crise

    Bevilaqua

    UniveNidade

    Estaduat

    paulisla.

    lnstiruto de

    euirnica.

    l).parl

    nento

    de Bioquimica

    e

    Tecnologia

    euimic ,

    Araraquara

    Sp, Brazil

    l)omingo

    Cantero

    Universidad

    de

    Ciidiz.

    Crdiz,

    Spain.

    l'rtricia

    Chiacchiarini

    Faculiad

    de

    tngenieria.

    Universidad

    Nacionnt

    dct

    (

    (nnrhue.

    Neuquan,

    Argenrina.

    l)nvid

    C.

    Dixon

    Department

    of

    Marerinls Engineclins.

    University

    of Bri(ish

    1 i)lunrbia.

    Vancouver

    Cxn.dr

    lr(l,anrdo

    Donati

    Cir)dcl'i

    (CoNl(

    lll tlNI-1,).

    U[ivcrsidrd

    Nlcxn

    t

    dc

    r_r

    Ptnri,

    L

    lrl

    rx.

    Ar8cnli

    r.

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    Crrlos

    Gentina

    School

    of

    Biochcrnicli

    Etrgireerit)g

    Pontilical

    Crtholic

    Univemity

    of

    valpataiso,

    valparaiso,

    Chil'

    Alejandra

    Giaveno

    Faculiad

    de

    Ingenieria'

    llnivcrsidad

    Nacional

    del

    Comahue'

    Neuqu6n,

    Argenlinn.

    Nicolas

    Guiliani

    Unit

    of

    Bacieri'tl

    Ceu

    Cornmuniadon

    Laboratory

    of

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    md

    Biotechnologv

    DeprimeDl

    of

    Biologv

    Frcuhy

    of

    Sciences'

    University

    of

    Chile.

    Sanliago'

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    Jose

    Manuel

    G6mez

    Monles

    de

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    Univenidad

    de

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    tretisa

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    u,."uJ

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    Uniaersidad

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    de

    Madrid

    Madrid'

    Sprin.

    I(.

    Hanumantha

    Rro

    Division

    of

    Mineral

    Processing'

    Lulei

    Universilv

    of

    Technology,

    Lulei.

    Sweden'

    David

    S.

    Holmes

    Center

    of

    Bioinformatics

    anit

    Genome

    Biologv

    Andr6s

    Bello

    U^t"-ui"tUaeul,

    rna

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