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CALCULATION
Nº M40000-4100-110-CAL-0001For
SULPHIDE ORE PROCESSING OPEX DERIVATION
Prepared by
CEJV – Casale EPCM Jo!" Ve!"#$e AMEC - %l#o$
Approved by
Discipline Leader: Pierre Lacombe (PL)
Functional Leader: Pierre Lacombe (PL)
Project Engineer: Juan Pablo Klimpel (JPK)
Area anager!Process anager: "oberto Aburto ("A)
Engineering anager: #arlos $arvae% (#$&)
Project anager EP: Paul c"ae (P)
#lient: ()
Re&' Da"e P#$(ose o) Re&so! P$e(a$e* C+e,e* A(($o&e* A Dec ' '*++ #EJ, Engineering #lose-.ut / PL PL
#omments:
0**+12+*13doc
COMPA.IA MINERA CASALE
PROJECT Nº M40000CERRO CASALE PROJECT
EPCM
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TA/LE O% CONTENTS
+3* 4$5".D6#54.$ 0
'3* 7#.PE0
03* "EFE"E$#E7 8
93* 76A" 8
83* DE,EL.PE$5 1
TABLES
5able 9-+: 7ummary o; Average 7ulp<ide .re Processing #osts = by #ost 5ype2
5able 9-': 7ummary o; Average 7ulp<ide .re Processing #osts = by #ost Area
5able 9-0: early 7ulp<ide .re Plant .perating #ost >5able 8-+: #ross 7ection o; Labour ont<ly 7alaries (Fully ?urdened) +*
5able 8-': 7ite-7peci;ic Electricity Pricing and .;;-7ite 5ransmission Losses ++
5able 8-0: $ameplate-7peci;ic .n-7ite 5rans;ormation @ 5ransmission Losses ++
5able 8-9: Electrical otor E;;iciency 5able +'
5able 8-8: Flotation Plant anpoer #osts ?reaBdon +0
5able 8-2: #rus<er and &rinding ill Liner and edia #osts +9
5able 8-: Abrasion 4ndices and ine "eserve Proportions per "ocB 5ype +8
5able 8->: Abrasion 4ndices and Poer 4ntensity per &rinding 7tage +8
5able 8-1: 7ulp<ide .re "eagent #osts +>
5able 8-+*: 7ulp<ide .re Processing Electrical Loads and #osts by .perations Area '*
5able 8-++: Parameters Applied ;or aintenance aterial #osts Derivation ''
5able 8-+': 7ummary o; Fres< Cater Distribution Processing #osts = by #ost 5ype '85able 8-+0: Fres< Cater Distribution 7ystem = Distribution o; Direct #osts over L. '2
5able 8-+9: 7ummary o; Lime 7laBing 7ystem Processing #osts = by #ost 5ype '2
5able 8-+8: Lime 7laBing 7ystem = Distribution o; #osts over L. '2
5able 8-+2: 7A"5 #ircuit = Distribution o; #osts over L. (be;ore $a#$ credits) '
5able 8-+: #osts and #redits "elated to #4L 6se o; 7A"5 #ircuit '>
5able 8-+>: &old "ecovery #ircuits #osts = Distribution o; #osts over L. '>
5able 8-+1: #osts "elated to #4L #ircuit 6se o; AD"!EC!"e;ining #ircuits '>
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1'0 INTRODUCTION
5<is document details t<e inputs and assumptions used to derive t<e processingoperating costs (.PE) ;or t<e sulp<ide ore o; t<e #erro #asale Project as presented
to ## ;or updating t<e ;inancial model <ic< along it< t<e revised capital costs
(#APE) estimate issued in ay '*++3
7ince t<e costs ;or t<ese circuits are s<ared at t<e onset beteen t<e processing o;
oide (by <eap leac<ing) and sulp<ide ore (t<roug< leac<ing o; t<e ;lotation cleaner
tails ;or recovery o; precious metals) t<e costs are presented on a yearly basis as ell
as on an average basis3
5<e average overall operating cost ;or t<e #erro #asale property is 67G311!t o;
sulp<ide ore3 5<ese costs are representative o; H+-'*++ pricing in 6nites 7tates o; America dollars (67G)3 5<e average costs relate to t<e processing o; sulp<ide ore
(and <ere applicable because o; cost s<aring ;or oide ore as ell) at t<e yearly
nominal t<roug<put and average ;eed grades3
5<e ec<ange rate used ;or t<e operating costs as 98 #<ilean Peso to 67 dollars
(#LP:67G)3 5<e bulB o; t<e operating costs eposed to ;oreign currency corresponds
to t<e labour costs3 7ome consumables are also costed in #LP namely t<e lime since
it is a local supply3
'0 SCOPE
.perating cost estimates ;or t<e ay '*++ revision o; ##I Financial odel ere
developed to a target accuracy o; -8 to +* generally based on ;irst-principles
assessment and parallel it< Bnon operations3 $eit<er escalation nor contingency
<ave been applied3 .perating costs ere derived as applicable ;or t<e ;irst uarter o;
'*++ by applying t<e ;olloing to t<e production ;orecast:
• mobile euipment <ourly operating costs
• labour reuirements
• ages and salaries
• grinding steel consumption adjusted to rocB type abrasion indices per empirical
euations• reagent consumptions per testorB or stoic<iometric relations<ips3
5<e processing ;acilitiesI costs are including t<e ;olloing aspects:
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• consumables (reagents poer lubricants ;uel grinding media comminution
euipment liners ;ilter clot<es) ;or t<e sulp<ide ore processing plant (e3g3
concentrator)
• manpoer ;or suc< plant ;or operation maintenance supervision and tec<nical
support
• maintenance parts and contractors
5<e costs speci;ically eclude any distribution o; general and administrative (&@A)
costs besides any direct burden to t<e base ages o; personnel and a cost
alloance to cover concentratorIs o;;ice and "@D epenses3
#osts ;or some areas outside o; t<e p<ysical con;ine o; t<e processing plant are also
included in t<e reported total alt<oug< not prepared nor revieed by Process3 5<ese
include t<e ;olloing aspects:
• port ;acilities costs eclusive o; concentrate loading sampling and assaying
costs (as arBeting costs)
• Piedra Pome% ;res< ater ell ;ield and ;res< ater pipeline operations (data
provided by ?rass-5ec<int)
• delivery o; concentrate ;rom concentrator to port ;acilities via pipeline (data
provided by ?rass-5ec<int)
• process ater recovery ;rom tailings pond (data provided by Arcadis)
• operation o; t<e reverse osmosis plant (C5P) at mine site and at port site (dataprovided by AE# #ade)
• operation o; regenerative poer plant on ;res< ater pipeline (data provided by
AE# #ade)
5rans;ers o; costs ;rom circuits s<ared it< oide processing are included in t<e
sulp<ide ore processing costs3 5<ese s<ared costs include t<e operation o; t<e
AD"!EC!gold re;ining and 7A"5 circuits3 5<e total costs related to t<ese circuits and
t<e distribution made to t<e sulp<ide ore processing ;acilities are detailed in document
9****-9+0*-++*-#AL-***+3
7ome costs incurred it<in ;acilities operated by t<e ;lotation processing plant butused by ot<er customers are distributed bacB to t<e end consumers3 5<ese include:
• assaying costs (s<ared it< t<e mine and geology department as ell as it<some gold recovery circuits)
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• cyanide destruction costs (s<ared it< t<e 7A"5 circuit)
• t<e preparation o; milB o; lime in a centrali%ed location at t<e ;lotation plant (usedon t<e leac< pad and in t<e s<ared AD" circuit)
• ;res< ater system (used by mine ;or dust abatement and &@A ;or camps andpotable ater supply)3
5<e apportioning o; t<e total costs ;or eac< o; t<ese s<ared ;acilities is based on t<e
most appropriate parameter to use in eac< case:
• ;or t<e AD" operation t<e tonnes o; loaded carbon processed ;rom t<e #4L and
#4# circuit are used
• ;or t<e 7A"5 circuit t<e copper load contributed ;rom eac< o; t<e #4L tailings andbleed ;rom t<e barren leac< solution ;rom t<e <eap leac< pad is used
• ;or cyanide destruction t<e proportional load o; cyanide sent to t<e circuit ;rom t<e
7A"5 circuit and t<e #4L circuit is used
• ;or ;res< ater based on average consumption per end users
'0 RE%ERENCES
+3 eras odel EPCM Model (May-05-11).fmd
'3 #onsumables pricingM ?arricB 5oronto Procurement
03 obile euipment <ourly costsM ?arricB 7antiago ining Department
93 ine Plan spreads<eet CC_2011_MinePlan_CEJV_04-Mar-11 values.ls
83 7preads<eet EPCM-Plan! "PE# $a!a %&ee! 'ev. $.ls ;or calculation o; metal
production
23 9****-9+0*-++*-#AL-***+ = &old Plant!7A"5 .perating #osts
4'0 SUMMAR2
.perating costs ;or t<e processing plant ere establis<ed using reagent consumptions
indicated by testorB <ere available reagent pricing data supplied by ## design
in;ormation and suppliersI uotes3 ?enc<marBing against similar operations as used
;or comparison3
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5<e overall estimated costs are presented in 5able 9-+ per cost type and in 5able 9-'
per processing area3 5<roug<put t<is document <ere process operating costs are
noted in 67G!t processed t<ese costs relate to dry tonnes o; sulp<ide ore milled3 5<ere;erenced mine plan per Appendi A is calling ;or +*+838 t o; ore to be processed3
5<e costs re;lect s<aring o; some costs it< t<e oide ore processing by <eap leac<ing
(/L) in particular t<ose related to t<e operation o; t<e AD" gold re;inery and 7A"5
circuits3 .nce t<e /L operations ;inis< t<e ;ull amount o; t<e ;ied costs ;or t<e
circuits previously s<ared it< t<e oide ore processing reports to t<e ;lotation plant3
early ;luctuations are due to t<e variability o; average grades ore <ardness and
composite abrasion inde <ic< ill in;luence product volumes grinding poer dra
and grinding media and liner ear rates in a non-linear ;as<ion3
Ta3le 4-1 S#55a$6 o) A&e$a7e S#l(+*e O$e P$o,ess!7 Cos"s – 36 Cos" T6(e
I"e5 LOM US8M US89" ($o,esse*: o) "o"al
($o,ess!7 ,os"s
Liners 0'3* *3022 939
&rinding 7teel 18*3+ *3102 ++30
"eagents ++'831 +3+*1 +039
Fuel +31 *3*+> *3'
.t<er #onsumables +3 *3**' -
Poer 990'3' 93028 8'32
Labour 9223' *3981 838
#ontractors - etallurgy ++83' *3++0 +39aintenance 7pares @ aterials
- obile Euipment 0*3* *3*'1 *39
- Process Euipment >8932 *3>9' +*3+
Leases on obile Euipment 32 *3** *3+
.t<er #osts (non-itemi%ed ;orpipelines port ater treatment)
8132 *3*81 *3
S#3-To"al ;<4' ;'0= 100
#redits
- #$ recovered ;rom 7A"5 (''83*) (*3''')
- Fres< ater pipelinepoer
(1'3+) (*3*1+)
To"al ;'11>'1 ?'@@
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Ta3le 4- S#55a$6 o) A&e$a7e S#l(+*e O$e P$o,ess!7 Cos"s – 36 Cos" A$ea
P$o,ess!7 A$ea LOM US8M US89" ($o,esse*
: o) "o"al
($o,ess!7 ,os"sPrimary #rus<ing '9'31 *3'01 '31
7econdary #rus<ing 8*+3* *3910 831
5ertiary #rus<ing ++1'32 +3+9 +93+
&rinding 099031 0301+ 9*3>
Flotation +'213* +3'8* +83*
Deatering @ Port '1131 *3'18 032
#arbon-in-Leac< (#4L) 1>03> *3121 ++3
5ailings 7torage Facility (57F) +023> *3+08 +32
Cater 5reatment at ine 7ite 923+ *3*98 *38
Cater 5reatment at Port 23 *3** *3+
.ver<eads 0+*38 *30*2 03
S#3-To"al ;<4' ;'0= 100
#redits (#$ ;rom 7A"5 poer;rom ;res< ater pipeline)
(0+3+) (*30+0)
To"al ;<11>'1 ?'@@
5<e costs incurred prior to t<e beginning o; t<e concentrator operations in H+ o; ear
9 <ave been de;ined in ##Is ;inancial model as representing .nerIs costs3 5<e
total costs incurred be;ore t<is moment (it< ear + o; t<e L. calendar re;lecting t<e
beginning o; mining activities) totalling 67G '132 <ave t<us been trans;erred out o;
t<e processing costs3 5<is e;;ectively reduces t<e reported L. unit cost ;or t<esulp<ide ore by 67G*3**0!t ;rom t<e 67G311'!t s<o in 5able 9-+ and 5able 9-'3
4n 5able 9-+ and 5able 9-' t<e trans;erred allocations ;or use o; common circuits suc<
as gold stripping circuit (AD") gold re;inery 7A"5 circuit and ;res< ater supply are
distributed under t<e various items ;or t<e sulp<ide processing plant3 4n 5able 9-' t<e
portion o; t<e costs ;or common use it< t<e /L ;acilities o; t<e AD" re;inery and
7A"5 circuits as ell as all o; t<ose related to t<e cyanide destruction circuit appear
under t<e #4L area3
5<e credits are s<on on separate lines but it< t<e cyanide recovered ;rom t<e 7A"5
circuit really reducing t<e net costs o; operating t<e #4L circuit <ile t<e poer generation credit ;rom use o; ;res< ater is delegated to t<e ;lotation circuit3
5<e .t<er #osts item in 5able 9-+ includes items suc< as ;res< ater and
concentrate pipeline operations (as costed by ?rass-5ec<int) ater treatment plants
by reverse osmosis at mine site and port3 A value o; 67G*3'''!t o; t<e total credits o;
67G*30+0!t represents t<e cyanide recovered t<roug< t<e use o; t<e 7A"5 circuit3
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5<e balance stems ;rom t<e generation o; electricity by t<e turbine installed in t<e
;res< ater pipeline3
.ver<eads include t<e supervisory and tec<nical personnel salaries not dedicated to a
speci;ic operating area o;;ice epenses as ell as general ependitures suc< as
researc< and development ("@D)3
5able 9-0 re;lects t<e yearly processing costs projected ;rom t<e detailed eras model3
Ta3le 4- 2ea$l6 S#l(+*e O$e Pla!" O(e$a"!7 Cos"
2ea$ S#l(+*e O$e
P$o,ess!7 Cos" US89"B9 = H+ ++3++
9 = H' >31'9 = H0 >3
9 = H9 >3+
8 >3'*
2 319
312
> >3**
1 311
+* >3*'
++ 310
+' 3>>
+0 3>8+9 3>0
+8 3>*
+2 3>'
+ 3>+
+> 31
+1 3>*
'* 3>
'+ >3+1
5<e ;olloing sections describe t<e met<odology used to estimate eac< processingcost item and t<e underlying assumptions3 Appendi & is presenting various detailedcost tables per area etracted ;rom t<e detailed eras model3
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='0 DEVELOPMENT
='1 /ass o) Es"5a"e.perating cost estimates ;or t<e '*++ ;inancial model revision ere developed to a
target accuracy o; -8 to +* based on ;irst-principles assessment and Bnon
operations3 $eit<er escalation nor contingency <ave been applied3 .perating costs
ere derived as applicable ;or t<e ;irst uarter o; '*++ by applying t<e ;olloing to t<e
production ;orecast:
• mobile euipment productivities and euipment!circuit availabilities
• labour reuirements
• ages and salaries
• reagent consumptions per testorB or stoic<iometric relations<ips3
5<e overall operating costs structure as establis<ed in a eras-based model3 5<e
model allos advanced auditing capabilities tracBing t<e sources o; t<e data used to
derive t<e operating costs as ell as sorting t<ese by type and area3 7tatistics o;
consumption o; t<e major consumables per period are also available as an output3
5<e processing costs ere developed ;rom t<e detailed mine plan and calculated
metal production sc<edule (see Appendi A) based on recovery projections
establis<ed per rocB type and variable it< <ead grades3 5<e main metallurgical
parameters are s<on in Appendi ?3
7upport labour it<in t<e processing operations as determined by engineering using
estimates o; activities3 5<e operating costs ;or ancillary mobile euipment include
suc< items as poer or ;uel tires lubricants and spare parts3
Process euipment costs are based on installed poer it< individual load ;actors
assigned to re;lect utili%ation rate as indicated by t<e euipment list3
aintenance costs ;or ancillary euipment are based on estimated euipment <ours
<ourly euipment operating rates estimates o; mec<anical availabilities and
maintenance labour intensities ;or eac< ;leet type as determined by ##Is ining
personnel3 5<ese ;actors ere adjusted over t<e li;e o; t<e euipment to re;lect t<eage o; t<e units3
For t<e processing plant euipment maintenance parts and materials are ;actored as
a ;raction o; t<e capital costs related to t<e purc<ase o; euipment (mec<anical
electrical instrumentation piping cabling cable and piping supports lig<t steel and
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building all s<ells)3 Eceptions are made o; t<e comminution circuits ;or <ic< t<e
yearly sum budgeted ;or maintenance as derived ;rom ;irst principles and ;or t<e
comminution euipment liners <ic< ere costed on t<e basis o; anticipatedreplacement ;reuency eig<t o; lining sets and steel price3
&@A costs are ecluded ;rom t<e scope o; t<is estimate3
='1'1 a7es a!* Sala$es
Cage and salary guidance as obtained by ## ;rom a #<ilean consultant using a
;irst uarter '**1 job classi;ications and rates survey3 5<e survey as conducted
across several current #<ilean mining operations3 ## indicated t<at t<e same rates
could be maintained ;or t<is cost estimating eercise it< an update to t<e .nersI
currency ec<ange rate guidance ;or .PE estimate ;rom #<ilean Pesos to 6373dollars (#LP98!67G+) and using t<e 8t< percentile o; t<e ;ully burdened peaB L.
rates as salaries3 Data ;rom t<e survey provided ;ully-loaded rates built up ;rom ;ive
di;;erent levels3 Cit<in eac< salary level t<ere are several rate categories all o; <ic<
include bonuses <ealt< insurance and pension alloance3
5<e ;ully-loaded rates ere increased ;urt<er to ;ully-burdened rates by adding
company salary burdens including some #<ilean-speci;ic statutory additions
severance and disability payments3
7ample salaries are provided in 5able 8-+3
Ta3le =-4 C$oss Se,"o! o) La3o#$ Mo!"+l6 Sala$es %#ll6 /#$*e!e*B
Pos"o!%#ll6 /#$*e!e* Mo!"+l6 Sala$es CLP8B
P=0 P>0 P?=
Process anager +*1+2'92 ++*8*891 +++>9>8+
Plant 7uperintendent 232981>' '*'20* 81'
aintenance 7uperintendent 2>0**8 *92*01 0*1*0
7enior etallurgist 921>2*0 8+*9*'2 88*1991
Plant 7upervisor 0898'9' 02>+1+* 0>+>81
anagement 7ecretary '*9'+1 '+>*190 '0+12>1
Primary #rus<er .perator +>12*8 '+*+802 '0*2115ailings 7ystem .perator ++28 +>82>0> +1181++
Celder +>882*0 '*+'08 '+21+++
&eneral Labourer +'8>0'' +0909'1 +9'>802
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='1' o$ S,+e*#les
5<e orB sc<edule assumes mine production and processing ;acilities ill operate
'9 <!d d!B 028 d!a3 .perations and mining personnel ill orB to +'-<our s<i;ts3
/ourly (non-eempt) personnel orB a -days-in!-days-out rotation3 7alaried
(eempt) personnel ill orB a +' <!d s<i;t on an >-days-in!2-days-out rotation3
anagement personnel (general supervisor level and up) ill orB day s<i;ts on a 9-
days-in!0-days-out rotation it< rotating eeBend coverage3 5ec<nical support sta;;
ill orB t<e day s<i;t only ;olloing a rotational roster3
='1' Ele,"$,"6 Cos"s
5<e unit price ;or electricity provided by ## as used to develop t<e poer cost ;or t<e process euipment3 5<ree prices are applicable plus t<ree levels o; o;;-site
transmission losses as s<on in 5able 8-'3
Ta3le =-= S"e-S(e,), Ele,"$,"6 P$,!7 a!* O))-S"e T$a!s5sso! Losses
S"eEle,"$,"6 Cos"
US89MB
O))-S"e T$a!s5sso!Losses
: o) (oe$ ,o!s#5e*B
#erro #asale ine 7ite 11 +39*
Piedra PNme% Cell Field ++8 +30
Port 7ite +8' *31'
,arious levels o; on-site trans;ormation and transmission losses are applicable
depending on t<e voltage o; t<e motor di;;erentiated by t<e nameplate capacity in
5able 8-03
Ta3le =-> Na5e(la"e-S(e,), O!-S"e T$a!s)o$5a"o! T$a!s5sso! Losses
S"e Mo"o$ Na5e(la"e BO!-S"e T$a!s5sso! a!* T$a!s)o$5a"o!
Losses : o) (oe$ ,o!s#5e*B
#erro #asale ine7ite
O +28 *382
+28 - O 9*** *391
9*** *3'
Piedra PNme% CellsField
O +28 *311
+28 - O 9*** *312
9*** *30
Port 7iteO +28 *3*2
+28 - O 9*** *3*0
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5<e sulp<ide processing plantIs electrical costs are based on t<e detailed euipment
list3 Assignment o; operating load per item it< consideration ;or calculated average
demand versus installed poer base ;or crus<ers mills pumps and conveyor motorsincluding circuit utili%ation provided t<e average total mec<anical demand3 5o t<is
value t<e motor electrical e;;iciency ;actor (per motor si%e ;rom 5able 8-9) o;;-site
transmission losses (;rom 5able 8-') and on-site losses (;rom 5able 8-0) ere added to
derive a net payable consumption3 5<ese data are provided in t<e mec<anical
euipment list in Appendi D3 5<e resulting poer costs are based on t<e average ore
<ardness ;eed grades and nominal plant t<roug<put3
Ta3le =-? Ele,"$,al Mo"o$ E)),e!,6 Ta3le
Mo"o$ Na5e(la"eB
E)),e!,6:B
Q9** 13*O9** = Q++* 123*
O++* = Q88 183*
O88 = Q98 193*
O98 = Q0* 103*
O0* = Q'' 1'3*
O'' = Q+8 1+3*
O+8 = Q++ 1*3*
O++ = Q38 >13*
O38 = Q838 >3*
O838 = Q9 >23*
O9 = Q'3' >03*
O'3' = Q+38 >3*
O+38 = Q*388 93*
*388 +3*
=' %lo"a"o! Pla!" Pe$so!!el
5<e salary levels ;or sta;; operations and maintenance personnel are based on
in;ormation provided by ##3 5<e individual ;ully-burdened ages ere derived ;rom
t<e classi;ication system provided by ##3
5<e total number o; sta;; is comparable to levels at similar large scale porp<yryoperations in #<ile it< adjustments ;or t<e plant con;iguration and t<e <ig< altitude at
#erro #asale3
5<e operations cres ill provide '9! coverage3 aintenance cres ill orB on day
s<i;t only ecept ;or a cre o; one supervisor it< ;our millrig<ts and ;our <elpers
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assigned on a rotation basis on nig<t s<i;t duty ;or plant emergencies covering bot<
t<e concentrator and gold plant3
7ome o; t<e personnel assigned to duties suc< as reagent preparation tailings
disc<arge to t<e pond and janitorial duties ill orB a 9-days-on!9-days-o;; sc<edule3
5<e number o; people in t<e maintenance department is consistent it< an operating
p<ilosop<y t<at plans to use contractors ;or t<e majority o; t<e repetitive major
maintenance tasBs3 5<ese ill generally be per;ormed <en t<e plant is s<ut don ;or
planned maintenance3
A breaBdon o; t<e number o; persons covering t<e various processing department
;unctions and related operating costs is provided in 5able 8-83
Ta3le =-; %lo"a"o! Pla!" Ma!(oe$ Cos"s /$ea*o!
A$eaN#53e$ o) E5(lo6ees
anagement @ Administration '
.perations +9*
Pipelines '0
5ailings 7torage Facility +*
Cater 5reatment Plant 9
aintenance - mill 57F port +'1
etallurgy '8
Assay laboratory 09
S#3-To"al ??
=' Co!s#5a3les
5<e price o; consumables as provided by ## (see Appendi E) or obtained ;rom
euipment bids recent uotes or ot<er #<ilean projects3 Pricing is based on
delivered product at site3 C<ere reuired t<e base price is increased by a
transportation c<arge euivalent to 67G0*3**!t3 $o import duties ere applied as it
as assumed t<at all items ill enter t<e country duty ;ree ;rom countries t<at <ave
;ree trade agreements it< #<ile3
5<e epected consumption is derived ;rom testorB data interpretation based on
establis<ed empirical euations or benc<marBing3
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=''1 Co55!#"o! EF#(5e!" ea$ S"eel
5<e ear steel costs associated it< t<e crus<ing grinding regrinding and limepreparation duties are s<on in 5able 8-23
5<e lime slaBer ear steel costs are net o; t<e credits received ;rom t<e /L operations
amounting to 67G*3**0!t o; sulp<ide ore over t<e L.3
Ta3le =-@ C$#s+e$ a!* G$!*!7 Mll L!e$ a!* Me*a Cos"s
I"e5P#$,+ase P$,e
US89"Co!s#5("o!
79"U!" Cos"
US89"
L!e$s
Primary crus<er 9881 038 *3*+2
7econdary crus<er 9+1+ +93 *3*2'5ertiary crus<er na na *3+>1+
?all mill '2>9 0+ *3*>'
"egrind mill '32>9 239 *3*+
Lime slaBer '02 *309 *3**+
G$!*!7 Me*a
?all mill +*80 >2* *31*2
"egrind mill ++0> ''38 *3*'2
Lime slaBer ++0> 831 *3**
S#3-To"al 1'0=
#redits (;rom /L = limeslaBing)
(*3**0)
To"al 1'0
$otes: + ?ased on roll li;e o; 9>** <ours +3+> Euro per roll pair and 67G+:*39 Euro3
Crusher Liners
5<e crus<er liner ear rates ere derived by considering t<e ;reuency o; replacement
;or t<e liner parts ;or t<e gyratory and secondary crus<ers and t<e estimated eig<t o;
t<e liner pieces3
5<e primary crus<er ear rate is based on replacing t<e concave and spider liners +38
times per year and replacing t<e mantle liners ;our times per year3 For ear rate
calculations ;or t<e secondary crus<ers one replacement every si eeBs isprogrammed ;or bot< t<e bol and mantle liners3
For t<e /P&" roll ear t<e interpretation o; t<e testorB data obtained by t<e
potential euipment vendor led to projecting a li;e o; 2>8* <ours3 5<is is based on
loer moisture content and a loer circulating load around t<e units t<an t<at
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anticipated ;or t<e scaled-up circuit o; #erro #asale3 5<ere;ore a;ter revieing
benc<marBing data a more conservative estimate o; 9>** <ours as used to
evaluate t<e liner costs3
Grinding Media and Liners
5<e grinding ball ear rates ere derived using t<e empirical ?ond euations
presented in Euations R8-+S3
?all and vertical mill media ear TBg!BC<U V *3+81 W (Ai = *3*+8)X REuation 8-+S
5<e ear rate euation reuires t<e abrasion inde (Ai) o; t<e materials being
processed3 5<ese ere obtained ;rom testorB per;ormed on rocB type composite
samples and are s<on in 5able 8- along it< t<e proportions o; t<e di;;erent rocB
types in t<e mine plan3
Ta3le =-10 A3$aso! I!*,es a!* M!e Rese$&e P$o(o$"o!s (e$ Ro, T6(e
Ro, T6(e A : o) M!e Rese$&es
&ranodioritic Porp<yry = &"D *390'2 +3'
Dioritic Porp<yry 7ulp<ide= DP *3'>89 '>3'
icrodiorite ?reccia = D? (sul andmi)
*308* +03+
,olcanic "ocBs = ,#&L,7 *3''8*+ 9+39
Ceig<ted Average *3'18+ -
$ote: + Ai ;or ,#&L and ,7 actually measured on a volcanic breccia sample
5<e resulting ear rates obtained ;rom Euation R8-+S epressed in eig<t o; abraded
material per unit o; energy input (Bg!BC<) ere t<en multiplied by t<e energy intensity
(in BC<!t) reuired to per;orm eac< o; t<e grinding duties3 5<is provided a unit steel
consumption (epressed in g!t o; ;eed to t<e milling stage)3 5<e parameters ;or eac<
grinding stage are s<on in 5able 8->3
Ta3le =-11 A3$aso! I!*,es a!* Poe$ I!"e!s"6 (e$ G$!*!7 S"a7e
G$!*!7 S"a7e APoe$ I!"e!s"66
+9" o) )ee* "o 5llB
Primary ?all ill *3'18+ +'399
"egrind ill*3+8*'
83>Lime Preparation ill *3*8*0 398
$ote: + Ai is t<e eig<ted value ;or t<e mine plan ore composition' ?enc<marBed ;rom similar duty at ot<er copper porp<yry plants0 Average value ;or nine limestone processors as reported by ?ond it< 0* discount ;or use
o; a ,ertiill
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9 Poer intensity ;rom ?ond euation ;or target grind si%e o; +'* Ym it< 8 reduction ;or micro-
cracBing ;rom /P&" pre-treatment: trans;er si%e ;rom et screening at a cut si%e o; +* mm o;
39 mm obtained ;rom simulations38 Poer input based on indicated average limestone ?Ci o; +*32 BC<!t P>* o; 98 Zm and 0*
poer discount ;or use o; ,ertiill32 Poer intensity epressed be;ore drive train transmission losses3
A credit o; 0* <as been applied against t<e ball consumption estimated using t<e
?ond euations ;or t<e use o; ;orged media in t<e plant instead o; t<e loer uality
cast type ;rom <ic< t<e ?ond empirical euations ere derived3 5<e indicated pricing
and ear rate ;or t<e ball mill media accounts ;or a maBe-up c<arge comprising to-
t<irds 1* mm diameter balls and one-t<ird 2* mm diameter balls3 ?ot< t<e regrind
mills and lime slaBer ill maBe use o; '* mm diameter balls3
5<e ball mill liner consumption derivation assumes a ;ull mill reline every +9 mont<s;rom benc<marBing o; large-diameter ball mills it< $i-/ard liners3 5<is euates to a
consumption o; 0+ g!t3
For t<e regrind ball mills t<e replacement sc<edule as also used to derive liner
costs3 5<is is based on a replacement ;reuency o; once per 0* mont<s3 4n t<is case
t<e Ai o; t<e material ;eeding t<e regrinding stage is unBnon and t<e empirical
euation cannot be applied3
5<e regrind mill ill be rubber-lined3 5<e unit cost (67G!t) ;or t<e consumed liners
ould liBely be euivalent to t<at ;or steel liners t<e loer consumption it< rubber
ould be ;ully compensated by t<e <ig<er purc<ase price3 5<e bene;its o; using
rubber are longer li;e easier <andling during relining and loer noise level in t<e
plant3
5<e liner consumption estimated ;or t<e lime slaBing duty using a ,ertiill is based on
t<e results ;rom t<e empirical euation (Euation R8-+S)3 5<e poer intensity (BC<!t)
used re;lects t<e <ig<er e;;iciency o; t<e ,ertiill set at * o; t<at o; an euivalent
ball mill3 5<e latter value is used to estimate t<e actual consumption rate o; balls and
liners3 5<is approac< results in an estimated consumption in line it< t<at indicated by
t<e liner c<ange ;reuency indicated by benc<marBing:
• .ne complete replacement o; all liners and scre liners per year
• .ne complete replacement o; t<e scre liners only per year
• 5o additional replacement o; t<e digging <eel (bottom scre liner) per year3
?udget uotes obtained ;rom comminution euipment bidders or ;rom ##Is .nersI
price guidance <en available ere used to calculate t<e grinding steel unit prices3
#onversion to tonnes o; mill ;eed ;or t<e regrind duty and t<e lime preparation mills
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as made based on t<e mass balance at t<e average ;eed grade ;or t<e regrind mill
and at lime consumptions o; +32' Bg!t o; ;lotation plant mill ;eed (combined ;lotation
#4L cyanide destruction circuits and allocated costs ;rom 7A"5 and gold recoverycircuits) and '3>+ Bg!t o; oide ore3 5<e consumption ;igures assume a uicBlime
supply it< 2 available #a. as indicated by data provided by ?arricBIs purc<asing
department3
='' Rea7e!"s
5<e reagent consumptions associated it< t<e ;lotation circuit are based on t<e
testorB program completed at t<e &@5 and 7&7 laboratories in '**> including t<e
pilot plant trials at 7&7 and consideration o; t<e additional orB completed at 7&7 in
'**13
"eagent use ;or t<e #4L circuit as derived ;rom testorB completed by 7&7 in '**13
Flocculant consumptions ere estimated ;rom t<icBening tests completed by .utotec
on pilot plant samples provided ;rom t<e 7&7 LaBe;ield testorB in '**>3 5<e use o;
#ibaIs agna;loc 08+ ;or all t<e plant-site reuirements is epected <ile t<e
consumption at t<e port site ill be covered by t<e slig<tly more e;;ective agna;loc
002 or t<eir euivalent ;rom anot<er provider3
5<e reagent consumptions ;or t<e cyanide destruction circuit are based on testorB
data obtained ;rom 7&7 orB in '**1 on #4L tailings3 5<e additional ;lo treated
t<roug< cyanide destruction ;rom t<e 7A"5 circuit neutrali%ation residue is minimal (interms o; overall cyanide load) and similar stoic<iometric reuirements ere used as ;or
t<e #4L slurry3 5<e stoic<iometric proportion o; sulp<ur present in sulp<ur dioide used
in t<e cyanide destruction circuit as converted into consumption o; elemental sulp<ur
(t<e reagent used to prepare t<e sulp<ur dioide solution) it< a conversion e;;iciency
o; >*3
5<e antiscalant addition rate is based on providing a concentration o; 8 ppm to t<e
process ater stream3 5<is is in t<e mid-range o; normal reuirements to so;ten
industrial ater according to t<e supplierIs tec<nical data s<eet3 5<e consumption is
based on a volume o; treated ater o; 81+ L!s (t<e average volume o; ;res< ater
introduced into t<e circuit)3
5<e detailed reagent pricing consumptions and costs are s<on in 5able 8-13 5<e
data include t<e trans;erred costs o; reagents used ;or t<e s<ared operation o; t<e
AD" and 7A"5 circuits it< t<e /L ;acilities3 5<ese circuit operations are detailed in
document 9****-9+0*-++*-#AL-***+3 5<e data do not include t<e reagents used in
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t<e ater treatment plants3 5<ese are appearing as [ot<er costs in 5able 9-+ as non-
itemi%ed cost components3
5able 8-1 re;lects t<e adjustment beteen t<e available #a. content o; t<e <ydrated
lime used in t<e testorB and t<at available to ## (at 2)3 5<ere is no credit
applied to t<e epected lime consumption ;rom <aving a large ;raction o; t<e process
ater recirculated (;rom t<icBener over;los) it< residual alBaline bu;;ering potential3
Ta3le =-1 S#l(+*e O$e Rea7e!" Cos"s
I"e5P#$,+ase
P$,eCo!s#5("o!
US89" ! 7$a5s ''' 79" 89"
%lo"a"o! C$,#" (e$ " o) (la!" )ee*
Lime +2838 >00 >00 *3+0>Primary collector (PA) '** 0* 0* *3*>+
7econdary collector (A09) '8** 0* 0* *3*8
et<yl 4sobutyl #arbinol(4?#)
'>28 +* +* *3*'
(e$ " o) $o#7+e$ ,o!,'#arboy-et<yl-#ellulose 1* +** +* *3*++
CIL C$,#"
(e$ " o) )lo"a"o! ,lea!e$ "al!7s
Lime +2838 +2+* +88 *3*'2
#yanide '0*1 +82> +8+ *309>
Activated carbon '+** '* +31 *3**9
5rans;er ;rom 7A"5 *3+1>5rans;er ;rom AD" *3*'1
Dea"e$!7 C$,#"s (e$ " o) ,o!,' o$ "al!7sFlocculant agna;loc 08+(concentrate at site)
0'** '* *3+ *3***
Flocculant agna;loc 002(concentrate at port)
0*1* +8 *3+ *3***
Flocculant agna;loc 08+(cleaner tailings)
0'** 98 932 *3*+0
Flocculant agna;loc 08+(roug<er tailings)
0'** 00 '1 *3*19
C6a!*e Des"$#,"o! (e$ " o) )lo"a"o! ,lea!e$ "al!7s7ulp<ur dioide (aselemental sulp<ur)
+9* '+'* '*+ *3*0
Lime +2838 +2** +8+ *3*'8
a"e$ T$ea"5e!" (e$ 53 o) )$es+ a"e$ Antiscalant ''** 8 +39 *3**0
To"al 1'10@
5<e net cyanide consumption associated it< t<e #4L circuit a;ter t<e credit ;or
cyanide recovered it<in t<e 7A"5 circuit (s<on as a separate line item in 5able 9-+)
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amounts to almost +3* Bg $a#$!t o; ;lotation cleaner tailings leac<ed vs3 t<e gross
consumption o; +38 Bg!t indicated in 5able 8-13 5<is credit amounting to 67G*3'''!t
decreases t<e total net cost o; t<e reagents used to process t<e sulp<ide ore to67G*3>>!t o; plant ;eed3
='' %#el Cos"s
A ;uel price as diesel o; 67G*3>!L delivered on site is used3 5<e total usage ;or t<e
mobile euipment ;leet assigned to t<e concentrator ;acilities or s<ared it< ot<er
users and ;or priming o; ;res< ater booster pump stations represents a cost o;
67G*3+>!t3
=''4 Assa6!7 S#((les
5<e assaying supplies cost as estimated based on t<e orB load epected in t<e
assay laboratory it< an average unit cost per sample assayed o; 67G'31*3
A daily load o; 0> samples as estimated3 5<is total is divided beteen t<e ;olloing
di;;erent clients:
• assaying o; production <ole drill cuttings grab samples ;or grade control and
geological samples ('8 samples)
• metallurgical accounting sampling (+* samples)
• on-stream analy%er calibration samples (+8 samples)
• metallurgical development orB samples eit<er ;rom plant surveys or ;romlaboratory scale testorB conducted in t<e metallurgical laboratory at site (8*samples)
• 7A"5 per;ormance samples (> samples)
• AD" per;ormance samples (+* samples)
• Environmental control samples (8 samples)
.; t<e daily total o; 0> samples >* samples per day are t<ere;ore allocated to t<e
process plant reuirements and a ;urt<er +> are s<ared beteen /L and concentrator
to ;ollo on t<e per;ormance o; t<e gold plant (+* samples) and 7A"5 circuit (>
samples)3
5<ose received ;rom t<e geological and mining groups are included in t<e total assay
supply cost o; 67G*3*01!t but are t<e source o; a credit to t<e concentrator o;
67G*3*'!t ;or assay supplies and t<e s<are o; t<e <ourly personnel salaries and
poer costs attributed bacB to t<ese departments3
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=''= %lo"a"o! Pla!" a!* A!,lla$6 Poe$ Co!s#5("o! Cos"s
5<e estimate o; installed poer actual operated loads and resulting cost byoperations area is s<on in 5able 8-+*3
Ta3le =-1 S#l(+*e O$e P$o,ess!7 Ele,"$,al Loa*s a!* Cos"s 36 O(e$a"o!s A$ea
Pla!" A$eaO(e$a"e*Loa* B
Ne" Loa*%a,"o$
Co!s#5e*Me,+a!,alLoa* B
U!" Cos"US89"B
Primary #rus<ing and .re"eclaim
++19 23 >+*8 *3+98
7econdary #rus<ing +908 839 +908 *3'2+
5ertiary #rus<ing 8*109 >3+ 01+ *300
&rinding ++100+ 1931 ++0'0> '3++0
Flotation and "egrinding '10*+ '32 '+'20 *30>*
.n-7ite #oncentrateDeatering
++9 8039 2+ *3**+
#oncentrate PipelineDeatering (port site) andLoading
020> 2238 '9+1 *3*2*
"eagent preparation +'2> 231 >2* *3*+8
#4L #ircuit 838'9 3> 9'1> *3*>
#$ Destruction +0+2 >031 ++*9 *3*'*
5ailings <andling '>>1 8130 ++9 *3*0+
"eclaim Cater 7ystem '> 223* 9>*+ *3*>2
Fres< Cater 7ystem '*'1> 2039 +'>' *3002
Cater treatment Plant at 7ite 1*8 283+ 8>1 *3*++
Plant 7ervices (aterdistribution air)
92>' >832 9**2 *3*'
Assay Laboratory 0'' >'3> +11 *3**0
#leaner 5ailings Pond"eclaim Cater
00* >'3> '0 *3**8
Cater 5reatment Plant at Port 0>+ 83* '>8 *3**0
To"al 9 A&e$a7e ?@<=1? ;'4: 0<1? 4'=
7<ared credit ;or poer generated ;rom t<e;res< ater pipeline
(*3*1+)
#redit ;or s<ared use o; assay lab ;res<ater pipeline ;rom mine /LM ;rom l imeslaBing ;or /L
(*3*9+)
5rans;er ;or s<are o; AD"!7A"5 circuitsoperation *3*89
To"al 4'?4
5<e total cost o; 67G93'9!t s<on in 5able 8-+* is to be compared it< t<e value o;
67G93028!t indicated in 5able 9-+ and to <ic< t<e credit o; 67G*3*1+!t ;or poer
generation by t<e ater pipeline is to be subtracted3
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=''> %lo"a"o! Pla!" Ma!"e!a!,e S#((les Ma"e$als Cos"s
Maintenance Materials and Equipment Spares
5<e calculation o; t<e spare parts cost is based on a yearly amount derived using t<e
#APE cost base represented by all process related euipment piping electrical and
instrumentation <ardare cabling pipe and cable trays lig<t structural steel and all
cladding o; buildings ;or eac< process area3
5<e amounts ;or t<e comminution circuits ere derived ;rom a ;irst-principles approac<
<ere individual pieces o; euipment ere analy%ed ;or t<e type o; replacement or
repairs reuired t<e ;reuency and t<e cost o; eac< repair in parts and materials3
ost major spare parts ere costed ;rom t<e pricing indicated in t<e budgetary
euipment bids received3 Additional contacts it< some vendors ere made to
complete t<e list o; parts reuired3
For t<e rest o; t<e plant areas a percentage as applied against t<e capital cost base
o; t<e euipment in eac< area3 5<e percentages vary beteen t<e various plant areas
re;lecting t<e type o; duty represented3
5able 8-++ indicates t<e parameters and t<e #APE per area3 5rans;er o; credits ;or
s<ared use o; t<e ;res< ater distribution system and lime preparation system as ell
as allocated costs ;rom use o; t<e AD" and 7A"5 circuits are accounted3 5<e
resulting unit cost ;rom applying t<e data in 5able 8-++ is a maintenance spares and
materials cost o; 67G*3>9!t3 5<is total ecludes spare parts ;or mobile euipment
maintenance reported separately (67G*3*'1!t) and related costs ;or pipeline andpoer generation turbine s<on under .t<er #osts in 5able 9-+ (67G*3*81!t)3
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Ta3le =-14 Pa$a5e"e$s A((le* )o$ Ma!"e!a!,e Ma"e$al Cos"s De$&a"o!
A$ea Rele&a!" CAPEX 8B US89"
Primary #rus<ing 0*>1910
*3*8+#oarse .re /andling +2228>'9
.re "eclaim +8>01'
7econdary #rus<ing ++1>19129 *3++2
5ertiary #rus<ing +818''180 *3+>
&rinding ++*9+'+2 *3'91
Flotation @ "egrinding 1192'1*1 *3++8
Deatering +'8291 *3*+0
Port Facilities (!o C5P) '11*191 *3*9*
"eagent Preparation 2>'8*11 *3**'
#4L '*8>'21 *3*9
#$ Destruction >811*1 *3**0
5ailings /andling ++''80*2 *3**8
"eclaim Cater '2+2221 *3**+
Fres< ater >0*88' *3**2
C5P (ine 7ite @ Port) ++019'> *3**8
Plant 7ervices3 01'*9++ -
To"al ?@?<0<?1 0';@
less credits (;res< ater l ime prep3) (*3**+)
allocated (AD" 7A"5) *3**9
To"al OPEX 0';4
Mobile Equipment Maintenance Costs
5<e costs ;or spare parts tires and lubricants to operate t<e ;leet o; mobile euipment
assigned to t<e mill as establis<ed as an <ourly cost based on benc<marBed data
it< utili%ation rates assigned to establis< actual ;uel consumption3 Eac< euipment
type is costed per t<e detailed cost s<eets developed per euipment type3
5<e age o; an operator ;rom t<e sur;ace cre ;or operation o; t<e maintenance crane
or t<e do%er on t<e coarse ore stocBpile <en reuired and t<e age o; a boom trucBoperator ;rom t<e maintenance cre eternal to t<e mill maintenance group ere
added to t<e processing costs as c<arges trans;erred ;rom t<ese departments3 Drivers
;or t<e personnel buses commuting beteen t<e mine and camp sites as ell as t<e
maintenance personnel assigned to maintain t<e buses also appear in t<e processing
costs3
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5<e resulting mobile euipment maintenance cost estimate s<on in 5able 9-+ is
67G*3*'1!t inclusive o; t<e AD" and 7A"5 circuit costs allocated to t<e concentrator3
Maintenance Contractors
A series o; repetitive maintenance tasBs ill be per;ormed during planned s<utdons
o; one grinding line or mill3 7ince t<ese are regular but in;reuent occurrences t<is
orB ill be assigned to contractors instead o; increasing t<e si%e o; t<e permanent
mill maintenance cre3
CorB <ours ;or contractors <ave been added into eac< sc<eduled s<ut-don period to
carry out major repair orB euipment rebuilds and structural repairs3 5<e tasBs are
analy%ed in 5able 8-+' it< estimates o; ;reuency cre si%e and tasB duration to
derive a total yearly cost3 A mobili%ation!demobili%ation alloance o; ;our <ours per trip
as built in alt<oug< it ould liBely be re;lected by <ig<er <ourly rates c<arged by t<e
contractor instead o; being an actual payment ;or <ours spent in transit3
A cost o; 67G+13'*!< ;or t<e millrig<ts and <elpers (provided by contractors) <as
been estimated ;rom ##Is age rates it< adjustments to t<e bene;its and t<e
addition o; pro;it3 7upervisors ere assigned a rate tice t<e rate ;or t<e cre
(67G0>39*!<)3
5rips by euipment vendor tec<nical representatives ere also included in t<is cost
category at 67G+'*3**!< (a miture o; local and out o; country support)3 A
mobili%ation!demobili%ation alloance o; +' <ours per trip as built in3 5ravel costs
are included in t<e administrative cost alloance3
5<e total ;or contracted maintenance is '999++ <ours per year or over ++ man-
years3
5<e breaBdon o; activities to be completed by or it< t<e assistance o; maintenance
contractors is s<on in Appendi /3 4t is estimated t<at a peaB cre o; almost '*0
persons can be epected on site <en simultaneous manpoer-intensive tasBs are
being undertaBen during partial or complete plant s<utdons3
5<e resulting contractual maintenance costs o; 67G*3**8!t are included in [.t<er
#osts\ in 5able 9-+3 5<e above total does not include t<e costs ;or t<e concentrateand ;res< ater pipeline maintenance <ic< are included under t<e yearly operating
costs o; t<ese ;acilities and appear as ell under t<e <eading [.t<er #osts\ in 5able 9-
+
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=''? a"e$ T$ea"5e!" Cos"s
An average ater treatment plant (C5P) cost o; 67G+30 per year <as beenestimated ;or t<e treatment o; an average o; +'* L!s o; Piedra PNme% ater o; <ic<
t<e reverse osmosis (".) permeate ill be released at t<e cut-o;; all marBing t<e
property aters<ed boundary and donstream aterays3 Cit< t<e variable yearly
;lorates indicated by t<e site ater balance accounting ;or variation in epected
aters<ed ater supply t<ese costs translate into a unit cost o; 67G*3*98!t o; sulp<ide
ore processed as s<on in t<e overvie in 5able 9-'3
5<e overall C5P costs are included in t<e sulp<ide plant processing costs divided
beteen manpoer reuirements electrical load reagents and maintenance spares
(including replacement o; t<e ". membranes every ;our years)3
Anot<er C5P is located at t<e port site treating t<e surplus process ater generated
;rom deatering t<e concentrate3 5<e reverse osmosis (".) plant is designed to
<andle up to 838 L!s o; ater at a cost o; 67G*3'+>!m 0 treated3 5<is is euivalent to
*3** G!t as reported in 5able 9-'3 5<ese costs are added to t<e sulp<ide ore
processing costs3
=''; P(el!es
5<e detailed operating costs provided by ?rass-5ec<int <ave been divided into
manpoer and electrical costs3 5<ese elements are s<on in t<e tables above eit<er
as part o; t<e ;res< ater system or t<e port and deatering ;or t<e concentratepipeline3 5<e balance o; t<e reuirements related to maintenance spares and
materials as ell as rig<t o; ay payments is s<on in 5able 9-+ as [.t<er #osts\3
5<ese residual costs ;or t<e concentrate pipeline amount to 67G28****!yr3 5<e costs
associated it< t<e ;res< ater pipeline add 67G+30!yr3 5<ese give a total unit cost
o; 67G*3*02!t o; sulp<ide ore processed3
=''@ O"+e$ Cos"s
Anot<er cost item appearing in t<e [.t<er #osts\ item o; 5able 9-+ is an alloance o;
67G8*****!yr ;or metallurgical and maintenance researc< and development ("@D)
programs3 5<is is ;or covering t<e costs o; projects per;ormed by or in cooperation
it< outside eperts3 5<is alloance adds less t<an 67G*3***8!t to t<e overall
processing plant costs3
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=''10 S+a$e* %a,l"es Cos"s
Fresh Water Distribution
5<e ;res< ater distribution system includes t<e poer and maintenance costs
associated it< t<e ell pumps booster pump stations and pipeline3 anpoer costs
and t<e total o; ot<er costs are split beteen t<e ;lotation plant t<e /L ;acilities and
t<e mine it< t<e >2 L!s consumed by t<e ater treatment plant included in t<e
;lotation plant costs3
5<e cost trans;erred to t<e mine and /L is based on t<e direct consumptions o; +13'
L!s and + L!s respectively ;rom an average total ;res< ater usage o; +2 L!s3 5<e
volume o; ;res< ater ;or t<e /L is mostly ater used ;or reagent preparation3 5<e
bulB o; t<e ater consumed ;or <eap irrigation is reclaimed ater ;rom t<e cleaner
tailings pond once t<e ;lotation plant is in operation3 Cater use ;or t<e preparation o;
s<ared circuits suc< as AD" and 7A"5 are c<arged to t<e ;lotation plant because o;
t<e limited volumes3
5able 8-+' gives a breaBdon o; t<e overall operating costs associated it< t<e ;res<
ater distribution system3
Ta3le =-1= S#55a$6 o) %$es+ a"e$ Ds"$3#"o! P$o,ess!7 Cos"s – 36 Cos" T6(e
I"e5 US8
Direct-/ire anpoer +890
Poer 00*9+Fuel '+28
aintenance Parts @ 7upplies 8+1*
Property Epenses (rig<t-o;-ay( +'2>
S#3-To"al ?4<>=
#redits ;or poer generation (191*+)
To"al ?@<?4B
5able 8-+' indicates t<at t<e ;res< ater distribution system costs over t<e L. ;or
all t<e identi;ied users total 67G093 5<is amount is t<en receiving a credit o;
67G1931 ;or t<e electrical poer generation enabled t<roug< operating a turbine ont<e last portion o; t<e ater pipeline3
5able 8-+0 is indicative o; <o t<ese costs are distributed amongst t<e main
consumers3
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Ta3le =-1> %$es+ a"e$ Ds"$3#"o! S6s"e5 – Ds"$3#"o! o) D$e," Cos"s o&e$ LOM
Use$ : o) To"al Cos"7ulp<ide Processing Plant 1*3>ine 93*/L 83'To"al 100'0
#redits ;or t<e poer generated ;rom t<e ;res< ater pipeline are assigned to t<e
sulp<ide processing plant and /L in t<eir respective proportions3
Lime Preparation Systems
5<e milB-o;- lime is prepared in a slaBing system providing t<is reagent to t<e ;lotation
plant and <eap leac<ing ;acilities3 5<e costs are included in t<e sulp<ide processingplant costs as manpoer electrical loads maintenance parts and liner and grinding
media as used in t<e lime slaBing mill3 5able 8-+9 provides a breaBdon o; t<e lime
preparation costs beteen users3 .ver t<e L. t<ese costs total 67G0'383
Ta3le =-1? S#55a$6 o) L5e Sla!7 S6s"e5 P$o,ess!7 Cos"s – 36 Cos" T6(e
I"e5 US8
Direct-/ire anpoer >>'9
Poer +88>1
.perating #onsumables
- Liners 10+
- &rinding balls 2>'1
aintenance Parts @ 7upplies 0*8
To"al <4??
Ta3le =-1; L5e Sla!7 S6s"e5 – Ds"$3#"o! o) Cos"s o&e$ LOM
Use$ : o) To"al Cos"Flotation #ircuit 903'#4L #ircuit 31#$ Destruction #ircuit 327A"5 #ircuit '83'
/L +23+To"al 100'0
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SA! Circuit
5<e total 7A"5 circuit operating costs are applied proportionally to t<e copper metalloads provided ;rom eit<er t<e #4# or t<e #4L circuit according to t<e mass balances
;or t<e ;lotation plant and leac< pad <ere consideration ;or grade variability and
dissolution rates ;or t<e copper values present is made3
5able 8-+2 establis<es t<e 7A"5 cost distribution over t<e L. beteen t<e sulp<ide
(#4L circuit) and oide (/L) ore processing ;acilities3 5<e L. cost to operate t<e
7A"5 circuit is 67G'293+ be;ore recovered cyanide credits3
Ta3le =-1@ SART C$,#" – Ds"$3#"o! o) Cos"s o&e$ LOM 3e)o$e NaCN ,$e*"sB
Use$ : o) To"al
Cos"#4L 1938/L 838
To"al 100'0
Despite t<at t<e #4L circuit is absorbing 1938 o; t<e 7A"5 circuit operating costs
over L. it is receiving only 30 o; t<e overall $a#$ credits o; 67G'1+
accumulated over t<e same period3 5<is is re;lecting t<e di;;erential dissolved copper
content solution volume and #$ad concentrations ;ound in t<e di;;erent streams sent
to t<e 7A"5 circuit ;rom eit<er t<e oide or sulp<ide processing circuits3 4n particular
t<e losses o; dissolved cupro-cyanates in t<e under;lo o; t<e #4L post-leac< t<icBener
contributes to t<is imbalance despite a <ig<er epected copper dissolution it<in t<e#4L circuit t<an on t<e leac< pad3
5<e copper units recovered it<in t<e 7A"5 circuit are not s<on as a credit against
t<e processing costs but as additional pay-metal production above t<at ;rom t<e
copper concentrate obtained by ;lotation3 /oever cyanide recovered it<in t<e
7A"5 circuit is treated as a credit against cost3 5<e copper recovery ;rom 7A"5 as
set at 18 and cyanide recovery at >38 based on testorB data3
5<e unit costs and production levels establis<ed ;or t<e L. average ;eed grades are
s<on in 5able 8-+3 .verall t<ere is a net credit o; 67G*3'1+!t o; sulp<ide ore ;or
using t<e 7A"5 circuit in addition to t<e value o; t<e copper produced3
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Ta3le =-0 Cos"s a!* C$e*"s Rela"e* "o CIL Use o) SART C$,#"
Cos"9C$e*" I"e5 U!" Ra"e
LOM
P$o*#,"o!
US89"
s#l(+*e
#ost = 7A"5 ;or copper recovery 67G93>'!lb #u 8+38 lb #u *3'92
#redit = #$ ;rom cupro-cyanate
dissociation in 7A"5+3*> Bg $a#$!Bg #u+ 199' t $a#$ (*30+0)
$ote: + ?ased on stoic<iometric ratio o; '30+ Bg $a#$!Bg o; #u reduced by #$Is 7A"5 recovery o; 1*
Gold eco"ery Plant
6nit costs ;or operating t<e carbon stripping and regeneration circuit (AD") gold
electroinning (EC) and re;ining are applied to t<e loaded carbon c<arges per
epected loading it<in t<e #4L and #4# circuits and according to t<e indicated
production rate per period per t<e mass balances ;or t<e ;lotation plant and leac< pad3
5able 8-+> illustrates t<e gold recovery circuits cost distribution over t<e L. beteen
t<e sulp<ide (#4L circuit) and oide (/L) ore processing ;acilities ;rom t<e overall
operating costs o; 67G+0+3 3
Ta3le =-1 Gol* Re,o&e$6 C$,#"s Cos"s – Ds"$3#"o! o) Cos"s o&e$ LOM
Use$ : o) To"al
Cos"#4L >038/L +238
To"al 100'0
5<e unit costs and production levels establis<ed ;or t<e L. average ;eed grades are
s<on in 5able 8-+13
Ta3le =- Cos"s Rela"e* "o CIL C$,#" Use o) ADR9E9Re)!!7 C$,#"s
U!" Ra"eLOM Gol*P$o*#,"o!
US89" s#l(+*e
8139 67G!o% 8380' Bg Au *3+*>
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APPENDIX A'
MINE PLAN
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APPENDIX /'
XERAS METALLURGICAL RECOVER2 PARAMETERS
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APPENDIX C'
XERAS /URDENED SALARIES STATISTICS %ROM SURVE2
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APPENDIX D'
EUIPMENT LOAD LIST
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APPENDIX E'
CONSUMA/LES PRICING
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APPENDIX %'
CAPEX DATA PER AREA %OR MATERIALS PARTS OPEX DERIVATION
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APPENDIX G'
XERAS MODEL OUTPUT TA/LES
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APPENDIX H'
CONTRACTUAL MAINTENANCE MANPOER /READON