PRE-FEASIBILITY RESULTS CONFIRM WORLD CLASS
PROSPECTS FOR APURIMAC PROJECT IN PERU
Strike Resources Limited is pleased to announce the completion of the Pre-Feasibility
Study (PFS) for its flagship Apurimac Iron Ore Project (the Project), in Peru.
The PFS, which took nearly a year to complete at a cost of approximately A$2.75
million, focused upon the development of a 20 million tonne per annum (20Mtpa)
mining operation with iron ore concentrate transported to the coast for shipment via a
slurry pipeline.
The PFS has confirmed that the Project has the potential to become a highly profitable
world class iron ore operation, with:
• Significant re-rating of resource inventory from JORC Inferred to JORC
Indicated of 133 million tonnes (Mt)
• Average operating costs of approximately US$14.5 per tonne
• Total capital cost of approximately US$2.3 billion
• High quality product grading +68%Fe, very low in Alumina, Phosphorous and
other impurities
If iron ore prices maintain their current levels, an operating cash surplus of
approximately US$1.44 billion is forecast for the first full year of production and
Project cash flows would be sufficient to repay the Project’s total capital cost within 2
years.
First production from the Project is scheduled for the first half of 2012. Strike is now
focussing on expanding its resource inventory in Apurimac and the commencement of a
Bankable Feasibility Study (BFS).
Commenting on the results of the PFS, Dr John Stephenson, Chairman of Strike said:
"The completion of the Pre-Feasibility Study for Strike's Apurimac Iron Ore Project in
Peru marks a major milestone for Strike and its Peruvian stakeholders. The
independent studies by consultants of world standing in their field, together with inhouse
analysis, has shown that the Apurimac Project alone has the capacity to deliver
to Strike and its shareholders a highly profitable long term source of cash flow. This
will be transforming for Strike, positioning it as a leading producer of high grade iron
ores, principally for the Asian market.
“I am extremely encouraged and excited by the results of this PFS and look forward to
the next phase in the Project's development. Strike is confident that substantially
more resources both at Apurimac and at Strike's other major Peruvian iron ore project
at Cuzco will be uncovered within the next twelve months."
20080723 SRK Pre-Feasibility Results Confirm World Class Prospects for Apurimac Project in Peru.doc
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DETAILS OF PRE-FEASIBILITY STUDY
In August 2007, Strike commenced its PFS programme, under the overall supervision of
Strike Director Professor Malcolm Richmond, to support a 20 Mtpa mining operation
from its Apurimac Project area. The PFS included a series of studies project managed
by Sinclair Knight Mertz (SKM). These studies covered the following broad areas:
Study Areas
STUDY PRIME RESPONSIBILITY
Geology, Mining and Resource Snowden Group
Mineralogy, Petrology and Characterisation CSIRO
Process system design and testing Sinclair Knight Merz
Plant and Site, Mechanical, Electrical, Power
Supply, Port and Mine
Sinclair Knight Merz
Infrastructure Mine and Port Sinclair Knight Merz
Port facilities Marine COSAPI S.A.
Pipeline Design Pipeline Systems Incorporated (PSI)
Community and Environment Sinclair Knight Merz
Risk Analysis Sinclair Knight Merz
Capital Cost Estimate and Operating Cost Estimate Sinclair Knight Merz
The results of these studies are summarised below:
OPERATING COSTS
Average operating costs (excluding contingency, royalty and depreciation charges) per
tonne of dry concentrate at full production are estimated (with an accuracy of +25%/-
10%) to be US$14.49 per tonne.
An additional provision for contingency or ‘risk’ costs has been estimated at $1.45 per
tonne.
Operating Costs
Cost US$/t Dry
Description Concentrate
Process, General and Administration 0.93
Reagents and Consumables 1.03
Infrastructure 0.40
Power 2.74
Spares 2.78
Mining and Geology 6.30
Port Operations 0.32
Total 14.50
Contingency 1.45
Total including Contingency 15.95
These operating costs are extremely competitive when compared with current and
planned producers in Australia. Furthermore, this competitive advantage is likely to
improve over time due to significantly higher inflationary pressures in the mining sector
in Northern Australia compared to that in Peru.
20080723 SRK Pre-Feasibility Results Confirm World Class Prospects for Apurimac Project in Peru.doc
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Operating Cost Comparison with Australian Iron Ore Companies
Company Cash costs before
royalties
A$/t FOB
Strike Resources (US$/t) 16
Fortescue Metals (FMG) – DSO 24
BHP (US$/t) 29
Rio Tinto (US$/t) 30
Midwest Corporation – DSO 38*
Murchison Metals – DSO 38*
Mount Gibson – DSO 42
Portman – DSO 42
Grange Resources – BFO 45
Gindalbie Metals - DSO 48
Source: BBY Limited (from Company Reports and Forecasts)
* Includes A$9 capital charge for rail and port
DSO = Direct Shipping Ore BFO = Beneficiated Feed Ore
CAPITAL COST ESTIMATES
Total direct and indirect costs for the project including engineering, procurement and
commissioning are estimated (with an accuracy of +25%/-10%) to be approximately
US$2.3 billion.
An additional provision for contingency or ‘risk’ costs (which also includes an allowance
for further possible savings, presently under review) has been estimated at US$200
million.
Capital Cost by area
Description Cost US$M
Mine Site and off site infrastructure 361,082
Process Plant 341,971
Tailings 4 8,329
Concentrate Pipeline 489,962
Port 280,962
Water Supply 3 4,886
Electrical and Communications 5 4,654
Total Indirects 692,765
Total 2,304,611
Contingency 200,555
Total incl. Contingency 2,505,166
Indirect costs include (among other items) an allowance for Engineering, Procurement,
Construction Management (EPCM), equipment freight and insurance, customs duties,
start-up and commissioning.
20080723 SRK Pre-Feasibility Results Confirm World Class Prospects for Apurimac Project in Peru.doc
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The capital cost estimates were developed from a detailed work breakdown structure
of each process, with costs for equipment based upon budget quotations from major
suppliers. A selection of contractors and suppliers were interviewed to compile
relevant information for setting applicable rates and costings. A field survey in Peru
was also completed, to check the correctness of rates.
FINANCIAL EVALUATION
Financial analysis by Strike confirms that the Project economics are potentially highly
attractive.
The capital and operating cost estimates from the studies, together with a conservative
assumption of an average price of US$60 FOB per tonne of concentrate, suggest the
Project will generate an operating cash surplus in the first full year of production of
approximately US$890 million. If iron prices maintain their current levels (equivalent
to approximately US$94 FOB), operating cash surplus in the first full year of production
is forecast to reach approximately US$1.44 billion and would be sufficient to repay the
Project’s capital cost within 2 years.
GEOLOGY AND RESOURCE
The focus of this study has been the Opaban I and Opaban III deposits, which were
previously announced by Strike to represent a JORC Inferred Resource of 172 million
tonnes at 62.28% Fe1.
The Resource Estimate by Snowden Group has now provided a significant re-rating of
the resource, from Inferred to Indicated status, delivering a total JORC Indicated
Resource of 133,530,000 tonnes, more than 93% of which has been included in the mine
plan.
JORC Indicated Resource Estimate
Location Tonnes Fe% AI2O3% SiO2% P% S%
Opaban I 125,000,000 59.26 2.12 7.87 0.04 0.14
Opaban III 8,530,000 62.08 1.37 4.58 0.07 0.25
Total/Average 133,530,000 59.40 2.07 7.66 0.04 0.15
The main Opaban I deposit is an iron-skarn deposit, tabular-shaped and generally flatlying.
Drilling has so far defined the dimensions of a mineralised body as being
approximately 1,600 metres long by 300 metres wide, in a zone in which massive iron
oxide deposits occur in several locations along a 5 kilometre northwest trend.
TRANSPORTATION
The transportation of ore will be by slurry pipeline from the mine site to the port. The
pipeline route has been determined and is 363 kilometres in length. This route is
shown in Annexure A.
The pipeline will consist of 26/22 inch diameter, unlined, API X70 steel pipeline with
two pump stations, one valve station and five choke stations.
1 Refer 23 August 2006: ASX market announcement titled “Peru Iron Ore Update on Apurimac
Project“and 19 July 2007: ASX market announcement titled “Apurimac Project - JORC Resource
Statement”
20080723 SRK Pre-Feasibility Results Confirm World Class Prospects for Apurimac Project in Peru.doc
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The pump stations will be located one at the mine site and one located 85 kilometres
along the pipeline route. The pump stations will provide the energy to transport the
concentrate through the pipeline.
The valve station will be required to isolate the pipeline system into two separate parts
when the pipeline is shut down, reducing the static head in the pipeline system to
approximately 4,000 metres of iron ore concentrate.
The chokes will be required to dissipate energy (dynamic head) in the pipeline as the
iron-ore concentrate descends from approximately 4,000 metres off the Peruvian
Altiplano.
MINING INFRASTRUCTURE
A conceptual mine study into the Opaban I and Opaban III resources has been developed
upon the basis that additional resource inventories are identified to support a
production rate of 20Mtpa over 20 years.
This study has provided:
• Conceptual pit designs and infrastructure
• Conceptual site layout, including location of main waste dump and haul
roads
• Conceptual mining schedule aimed at optimising value during the extraction
of the Opaban I and Opaban III resources and conceptual satellite deposits
• Estimation of operating costs and capital costs for the mining operation
Mine strip ratios have been estimated at 1.71 for Opaban I and 0.66 at Opaban III. A
more detailed geotechnical drilling programme will be required to ensure the correct
pit slope angle is used. A highly conservative angle of 35 degrees has been used for the
study, so the potential exists to steepen the slope and therefore reduce the strip ratio
and further reduce mining costs.
MINERALOGY, PETROLOGY AND CHARACTERISATION
CSIRO were commissioned to complete characterisation of the mineralogical and
petrological characteristics of iron oxides from the various ore types found in the
Opaban I deposit.
The work identified four important characteristics:
• The iron mineralogy is made up of 60% hematite and 40% magnetite
• The ore is coarse grained
• There is widespread internal fracturing within the grains
• The gangue minerals comprise silicates which are, relative to iron minerals,
very soft
20080723 SRK Pre-Feasibility Results Confirm World Class Prospects for Apurimac Project in Peru.doc
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Magnetic (low intensity and high intensity) test work on reverse circulation chip
samples was very successful and has returned product grades at coarse crushing with
particle sizes of 80% passing 125 and 250 microns as follows:
Metallurgical Test Work Results
Product Grade
Fe 68.02 % to 68.28%
Al2O3 0.30% to 0.35%
SiO2 1.51% to 1.77%
P 0.01% to 0.02%
These excellent results suggest low energy consumption for the beneficiation process,
which means lower operating costs. No floatation circuit is required as part of the
beneficiation process.
PROCESS SYSTEM DESIGN AND FLOW SHEET
The Process Flow Sheet developed by SKM is shown in Annexure B. The beneficiation
and production concept developed for the Opaban I and Opaban III ore bodies will
require:
• A Primary Gyratory Crusher for primary size reduction from minus 1000mm
maximum to a P80 of 90mm
• Secondary crushing and screening in closed circuit for feed size reduction
from a feed P80 of 90mm to a P80 of approximately 13mm
• High Pressure Grinding Rolls (HPGR) for the first stage of fines production
• Wet screening of HPGR product at 4mm in closed circuit
• Primary Ball mills for reduction to a P80 of 0.25mm
Since the run of mine (ROM) grade is a very high 57% Fe and the mineralogy is
conveniently interlocked magnetite/hematite, a simple two step magnetic separation
will produce a high grade product.
The two steps of magnetic separation will be as follows:
• Low Intensity Magnetic Separators (LIMS) for magnetite concentration
roughing and cleaning stages
• Wet High Intensity Magnetic Separators (WHIMS) for hematite concentration
from the LIMS tailings
The concentrates will be ground to 100% passing 150 microns and 80% passing 48
microns, thickened and transported as slurry to the port via pipeline. At the port they
will be dewatered (filtered) and stock piled for shipment.
An overall process route has been defined based upon the design tonnage of 20Mtpa of
dry concentrate grading approximately 68% Fe and a mass recovery from ROM feed of
70.3% based upon the expected head grade of 57% Fe.
20080723 SRK Pre-Feasibility Results Confirm World Class Prospects for Apurimac Project in Peru.doc
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PORT SITE
Port selection was based on the following principal considerations:
• The port site needs to be sheltered from prevailing weather conditions and
have a minimum of 20 metres water depth at low tides
• The land area for the port site needs to have adequate space for dewatering
facilities, stockpiles and residential buffer zone
• The wharf facility must accommodate a 7,000 – 10,000 tonne per hour
travelling shiploader, ship manoeuvring space, dolphins, buoys and
anchorage locations
• The site must be able to accommodate expansion to 40 Mtpa stockpiling,
loading and shipping
The bay of Tres Hermanas has been selected at the preferred location for the
establishment of the Port Facility.
Tres Hermanas has natural deep
water and a semi submerged reef
extending offshore, which offers
protection from the prevailing
weather.
Bathymetric studies, including
depth sounding and contour
plotting have confirmed the
suitability of the deep harbour.
A depth of 20 metres is available at
approximately 300 metres off
shore. Jet probing of the bay area
showed the sea bed to be several
metres of sand over a rock base.
Aerial photograph of Tres Hermanas Port Site Location
The conceptual design of the port at Tres Hermanas comprises:
• A rock fill breakwater based on the existing semi-submerged reef (thus
requiring minimum additional rock fill) on the southern boundary of the bay
• A steel and concrete wharf structure that supports a 7,000 tonne/hour ship
loader
• Mooring dolphins suitable for 150,000+ tonne cape sized vessels
• Service jetty for tug boat access
• Navigation aids and buoys
The land area at Tres Hermanas is relatively flat, devoid of any sort of vegetation and
is uninhabited. As such, it is highly suitable for the location of facilities to dewater,
stockpile and load product at a rate of 20 to 40 Mtpa.
Tres Hermanas is situated 13 kilometres from the town of San Juan and therefore
allows the workforce to live in an existing town close by.
20080723 SRK Pre-Feasibility Results Confirm World Class Prospects for Apurimac Project in Peru.doc
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PORT INFRASTRUCTURE
The main elements of Port Infrastructure will comprise:
• Filtration Plant
• Product Stacker
• Product Reclaimer
• Shiploader
The iron ore concentrate will be dewatered at the port through a filter system.
Concentrate will then be fed by conveyor belt to the product stacker, which will feed
on to the boom conveyor and discharge on to four stockpiles each holding
approximately 250,000 tonnes.
Stockpiled material will be reclaimed from the stockpiles by the Product Reclaimer and
fed to the Ship Loader.
POWER SUPPLY AND RETICULATION
Power requirements for the Project at the mine site and port will be serviced from
existing surplus capacity from the national grid system.
The power requirement for the mine site is estimated at 125MW and for the port site
14MW, both of which can be serviced through the construction of new transmission
lines to Peru’s main electricity grid.
For the mine site, connection to the grid will be via an existing substation at Cotaruse,
requiring approximately 100 kilometres of new transmission line to be constructed.
For the Port, connection to the grid will be at the Marcona Substation near San Nicolas
Port, requiring a new 30 kilometre transmission line.
WATER SUPPLY
The mine site is fortunate in its location in that there are large bodies of water nearby
and the region has high levels of rainfall. The estimated quantity of water required for
the mine site and pipeline operation is 17.8Mm3 (17.8 gigalitres) annually.
The preliminary water modelling indicates that available water resources will be
sufficient to cover the demands for both the plant and for concentrate transport to the
coast.
It is envisaged that the development of the water supply for the mine will also result in
significant improvements to the quantity and quality of water supply to the local
communities.
Works required to store and distribute water to the mine site will include the
construction of a small dam, charge tank, storage reservoir, pumping station and
pipeline.
The disposal of 12Mm3 (12 gigalitres) of water from the filter plant at the port presents
an opportunity for the Project to enhance sustainable agriculture in the region.
20080723 SRK Pre-Feasibility Results Confirm World Class Prospects for Apurimac Project in Peru.doc
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ENVIRONMENTAL AND COMMUNITIES
The Project faces the usual environmental and community risks to any project at this
development stage.
The biophysical environmental challenges of rehabilitation, water management, flora
and fauna, air, noise control and cultural heritage matters appear relatively
straightforward using proven industry practices to manage the impacts to acceptable
levels.
Establishment of trust between the project and the local regional communities will be
essential to address community concerns about the Project.
NEXT STEPS
With the positive results from the PFS, Strike is now aggressively targeting the
following key Project milestones;
• Expanding resource inventory in Apurimac to +300Mt (December 2008)
• Completion of Railway Scoping Study (September 2008)
• Completion of Bankable Feasibility Study (June 2009)
• First Production from Apurimac (first half of 2012)
Strike is investigating project alternatives to the central case described above,
including the use of contract mining (to reduce direct Project capital costs) and the use
of a railway instead of a slurry pipeline.
A Preliminary Scoping Study suggests that a railway for transporting sinter fines and
lump from the mine to the coast is technically feasible and would offer significant cost
savings at the mine beneficiation plant. Further work is currently underway to more
accurately analyse the value trade off. This work is expected to be completed by the
end of September 2008.
Strike notes that production from its Cuzco Lump Project is scheduled to commence
sooner than the Apurimac Project, as Strike is aiming to commence 1 to 2Mtpa of lump
production from its Cuzco Project area in 2009 to generate early cashflow.
Also, Strike notes the potential for an additional 20Mtpa production from the Cuzco
Project area. However the Cuzco area was outside the scope of this Pre-Feasibility
Study.
For further information:
John Stephenson Shanker Madan
Chairman Managing Director
T | (08) 9214 9700 T | (08) 9214 9700
E | [email protected] E | [email protected]
The information in this announcement that relates to Exploration Results, Mineral Resources or Ore Reserves has been
compiled by Mr Hem Shanker Madan who is a Member of The Australian Institute of Mining and Metallurgy. Mr Madan
is the Managing Director of the Company. Mr Madan has sufficient experience which is relevant to the style of
mineralisation and type of deposit under consideration and to the activity which he is undertaking, to qualify as a
Competent Person as defined in the 2004 Edition of the “Australasian Code for Reporting of Mineral Resources and Ore
Reserves (the JORC Code).” Mr Madan consents to the inclusion in this announcement of the matters based on his
information in the form and context in which it appears.
DATUM ELEV
0+000 10+000 20+000 30+000 40+000 50+000 60+000 70+000 80+000 90+000 100+000 110+000 120+000 130+000 140+000 150+000 160+000 170+000 180+000 190+000 200+000 210+000 220+000 230+000 240+000 250+000 260+000 270+000 280+000 290+000 300+000 310+000 320+000 330+000 340+000 350+000 360+000
3752.5
3700.0
3777.7
4204.1
4200.0
4039.9
3940.6
3944.7
3945.5
4020.6
3869.6
3623.5
3332.2
3564.4
3814.2
4000.0
4250.0
4408.0
4151.3
4250.0
4306.4
4372.3
4414.7
4471.5
4420.8
4480.9
4531.2
4500.0
4500.0
4513.0
4431.8
4400.0
4400.0
4316.6
4268.9
4194.8
4059.8
3881.1
3603.0
3229.9
2854.4
2481.5
2730.4
3439.1
3513.0
3978.0
4038.1
3884.3
3613.1
3355.7
2913.1
2729.8
2504.5
2372.6
2100.0
2009.7
1991.1
1805.0
1827.6
1677.4
1497.3
1285.0
1076.5
936.6
737.4
517.3
568.2
541.3
500.0
379.6
250.4
100.0
100.0
00.0
PUMP STATION 1
KP. 0+000
PUMP STATION 2
KP. 85+000
CHOKE STATION 1
KP. 240+000
CHOKE STATION 2
KP. 256+000
CHOKE STATION 3
KP. 286+000
TERMINAL STATION 1
KP. 363+000
CHOKE STATION 4
KP. 320+000
VALVE STATION 1
KP. 180+000
BY ROAD
CORRIDOR
BY ROAD
CORRIDOR
BY ROAD
CORRIDOR
ROAD
CORRIDOR
BY
ROAD
CORRIDOR
BY
Mine Site Location
Coordinates :
N 8,483,722.08; E 680,436.31
Elevation :
3837 MASL
Port
Legend
Pipeline Corridor (5 Km)
OPTION B-5
Panamerican Highway
Secondary Road
River
Department Limits
Province Limits
National Reserve
1.- TOPOGRAPHY INFORMATION PROVIDED BY INSTITUTO GEOGRÁFICO
NACIONAL DEL PERÚ (IGN).
2.- NATIONAL RESERVES PROVIDED BY INSTITUTO NACIONAL DE
RECURSOS NATURALES DEL PERÚ (INRENA).
3.- THE STARTING POINT (MINE SITE - OPABAN 1) AND THE LOCATION
OF THE 3 PORTS (DE LOMAS PORT, TRES HEMANAS PORT,
SAN JUAN PORT), IS PROVIDED BY THE CLIENT.
4.- COORDINATE SYSTEM ( WGS 1984 UTM Zone 18S).
PJP5209-DWG-PL-007 B
OPTION B-5
OPABAN 1 TO TRES HERMANAS PORT
PLAN & PROFILE
ISSUED 07/02/08 FOR INTERNAL REVIEW
ISSUED FOR CLIENT REVIEW
A
B
JLC JDR PFM
M. LETELIER J.L. CALIXTO INDICATED
OPTION B-5 - PROFILE
HORIZONTAL SCALE 1:600,000
VERTICAL SCALE 1:200,000
363+000
360+000
355+000
350+000
345+000
340+000
335+000
330+000
325+000
320+000
315+000
310+000
305+000
300+000
295+000
290+000
285+000
280+000
275+000
270+000
265+000
260+000
255+000
250+000
245+000
240+000
235+000
230+000
225+000
220+000
215+000
205+000
200+000
195+000
190+000
185+000
180+000
170+000
165+000
160+000
155+000
150+000
145+000
140+000
135+000
130+000
125+000
120+000
115+000
110+000
105+000
100+000
95+000
90+000
85+000
80+000
75+000
70+000
65+000
60+000
55+000
50+000
45+000
40+000
35+000
30+000
25+000
20+000
15+000
10+000
5+000
0+000
Puquio
PUMP STATION 1
Kp. 0+000
PUMP STATION 2
Kp. 85+000
CHOKE STATION 4
Kp. 320+000
CHOKE STATION 1
Kp. 240+000
CHOKE STATION 2
Kp. 256+000
CHOKE STATION 3
Kp. 286+000
TERMINAL STATION 1
Kp. 363+000
VALVE STATION 1
Kp. 180+000
OPABAN 1
De Lomas Port
Tres Hermanas
Port
San Juan
Port
Pampa Galeras
Barbara D'Achille
(National Reserve)
Cotahuasi
(National Reserve)
OPTION B-5
363 Km
LUCANAS
NAZCA
ICA
AYMARAES
PARINACOCHAS
CARAVELI
LA UNION
HUAYTARA
SUCRE
ANDAHUAYLAS
ABANCAY
PALPA
CARAVELI
HUANCA SANCOS
ANTABAMBA
VICTOR FAJARDO
GRAU
PAUCAR DEL SARA SARA
CONDESUYOS
VILCAS HUAMAN
CHINCHEROS
CANGALLO
CASTILLA
AYACUCHO
ICA
APURIMAC
AREQUIPA
AREQUIPA
HUANCAVELICA
TINTAY
TURPO
ANDAHUAYLAS
HUANCARAMA
CHAPIMARCA
PICHIRHUA
LUCRE
TOQUEBAMBA
SAN JUAN DE CHACÑA
HUANCARPUQUIO
JAQUI
Acarí
Bella Unión
San Nicolas
ANISO
UPAHUACHO
PACAPAUSA
SAN FRANCISCO DE REVACAYCO
CHAVIÑA
CHAQUIPAMPA HUISJATAGNA
ALHACONE
HUAYLLANE
CHANTANE
HUANCA HUANCA
PUQUIO
LUCANAS
S/N
SAN JUAN
SAN CRISTOBAL
SAN PEDRO
PUNCUHUAJA
SANTA ISABEL
SALSA
SAN ANDRES
SANTIAGO DE VADO
NASCA
NASCA
VISTA ALEGRE
PIRCA
SAN LUIS PAJONAL
CUPARA
SANTIAGO NUEVO
TAMBO QUEMADO
UCHUYMARCA
BUENAVISTA
UCHUYTAMBO
CHUQUIMARAN (DESTRUIDO)
YANACA
SORAYA
SAÑAYCA
ANCOBAMBA
CHALHUANCA
TORAYA
COTARUSE
CARAIBAMBA
HUAYLLO
COLCA
PAMPAMARCA
AYAHUAY
TIAPARO
POCOHUANCAPACHACONAS
TAPAIRIHUA
TINTAY
SORAS
APONGO
CABANA
CHIPAO
AUCARA
ANDAMARCA
SONDONDO
QUEROBAMBA
ISHUA
PAMPACHIRI
MORCOLLA
HUACAÑA
PAICO
POMACOCHA
QUECA
ASQUIPATA
MOYOBAMBA
RACJAYA
SANTA ANA DE HUAYCAHUACHO
SAN PEDRO DE LARCAY
SANTIAGO DE PAUCARA
JAHUAY
ACARI
LUCASI
EL TORO
AMATO
LA ENCAÑADA
NEGRA
MACHADO
PONGO
COLAPAMPA
HUAJUMA
ARENAL
TRANCA GRANDE
LOS CARACOLES
BEATITA
CHALCO
LA MUÑA
MILAGROSA
CELESTINA
LLUCYUCA
TOSO
PARAJE
PAMPA ALTA
MOCHILCO
EL PUENTE
DEGOLLADERO
SANTA ROSA
SEVILLANA
LOS RIFLES
DOS POZOS
LA LOZA
LOS ANGE LES
TRANCA BAJA
CUESTA DEL MOLINO
LLAMACHAYOC
COLORADO
PEDREGOSA
BUENAVISTA
LA MONJA
LA MANCHA
TORO MUERTO
SAN FRANCISCO
BRASIL
CUESTA BOTITANO
HUARANGUITO
GRANDE
SAN VICENTE
DESPENSA
LLANO LOMA
BATIDERO DESAGUE
LOS ESPINOS
CHALCO
ACARI
PONGO
ENNO
FILLO
ANCO
LAYO
PIRURO
PAICA
TISANI
PALLCCA
HUAYLLA
PAMPAHUASI
CHAGUAYA
CHUPA
PUICO
ACHUANE
CHAUPI
TIPICCOCHA
PALCA
COLLPA
LLOCA
PUCA
PASCANA
MUCCGA
PALLCA
PALLANCATA
RAYO
TINCOJ
COTANI
CANCALLA
CHACALLAU
CHUSPA
TACRA
LOLLOTA
ICHUMARCA
SAN JACINTO
PARARANI
UTCO
CAJUANE
CAHUIÑA
ANTACCOLLO
COCHAHUACHO
MAJLLA
DELLAMCAMA
OCCSALLAHUAYCCO
PILLONE
UCHACHA
ANGOSTURA
JUISAPATA
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NEGRO
QUILCACCASA
HUCAÑA
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TACCR A
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VERDE VERDE
PACCHETATA
PELLONE
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TOLORA
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CHOQUE
TUMACORCCO
COCHALOMA
SEÑUERE
HUAÑACACA
AZARANTA
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JIMENEZ
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ISCAHUACA
CHUNCURUMI
PISCAPUQUIO
YURACPACCHA
JAMAYACHI TORMINE
PALCASHERA
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PATAN
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BIOLANDO
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MATARA
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PARALMAYOC
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TRES CRUCES
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S/N
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PUCAJAJA
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S/N
APACHETA
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
ACARI
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
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S/N
ICHUORJO
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
PALLP O
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
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S/N
JALAORJO
ACARI
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
S/N
LUCANAS
ICA
CARAVELI
NAZCA
AYMARAES
PALPA
PALPA
NAZCA
CARAVELI
NAZCA
CARAVELI
CARAVELI
450,000
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8,300,000
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D R A W I N G S L I M I T S
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SCALE 1:500,000
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Last
2.9¢ |
Change
0.000(0.00%) |
Mkt cap ! $8.228M |
Open | High | Low | Value | Volume |
2.9¢ | 2.9¢ | 2.9¢ | $116 | 4K |
Buyers (Bids)
No. | Vol. | Price($) |
---|---|---|
1 | 143133 | 2.9¢ |
Sellers (Offers)
Price($) | Vol. | No. |
---|---|---|
3.2¢ | 25903 | 1 |
View Market Depth
No. | Vol. | Price($) |
---|---|---|
1 | 143133 | 0.029 |
3 | 200000 | 0.028 |
1 | 120000 | 0.026 |
1 | 40000 | 0.023 |
2 | 400888 | 0.021 |
Price($) | Vol. | No. |
---|---|---|
0.032 | 25903 | 1 |
0.033 | 98700 | 2 |
0.035 | 33662 | 1 |
0.036 | 30000 | 1 |
0.038 | 263157 | 1 |
Last trade - 13.00pm 19/09/2025 (20 minute delay) ? |
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SRK (ASX) Chart |