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    DMC Mining Limited 1
    23rd June 2008
    ASX/Media Announcement
    Scoping Study Complete – Mayoko Iron Ore Project
    The Directors of DMC Mining Limited (“DMC”) are pleased to release the findings of the
    Scoping Study completed by GRD Minproc Limited (“Minproc”) on DMC’s 80% owned
    Mayoko Iron Ore Project in The Republic of the Congo. The executive summary of the
    Scoping Study is attached to this announcement.
    KEY FINDINGS OF THE REPORT
    • Although the Mayoko Iron Ore Project is at a very early stage
    of development the preliminary economics appear attractive
    and therefore justify advancing to a more detailed level of
    assessment.
    • Direct shipping ore (DSO) production of 3Mt/a to commence as
    stage 1, and to increase to 11Mt/a within 4 years.
    • Existing rail capable of transporting 11Mt/a with minor
    upgrades.
    • Capital expenditure estimate of USD$198 million for 3 Mt/a
    DSOoperation.
    • Capital Expenditure estimate of an additional USD$288 million
    (USD$486 million total) to achieve 11Mt/a DSO operation.
    • Operating costs estimate of $22/tonne for 11Mt/a
    • Revenue potential of USD$1.1 billion/a based on 11Mt/a at
    current spot prices or USD$302 million /a based on 3Mt/a at
    current spot prices.
    • Timeline to production forecasted at 4 years to achieve 11Mt/a
    operation.
    The scoping study commenced in Feb 2008 and has involved over 1,500 man hours
    from GRD Minproc expended across mining, processing and infrastructure assessments.
    This included visits to the Republic of the Congo for discussions with the port, rail and
    power authorities. While the study does not meet Pre-feasibility Study standards it
    exceeds Scoping Study requirements with a number of key issues examined in
    considerably more detail than warranted for a Scoping Study.
    DMC Mining Limited 2
    Minproc has given consent to DMC to include the Executive Summary of the scoping
    study to this ASX announcement.
    Minproc’s assessment of mining and processing was based on the 33Mt Inferred
    Resource estimate previously reported by DMC. Haematite production would commence
    at 3 Mt/a and be ramped up to 11 Mt/a. Then, if necessary, the operation would
    produce nominally 3 Mt/a of pellets from the magnetite tonnage.
    The preliminary mine design modelling was based on a 55% Fe run-of-mine product
    and 50% Fe cut-off grade and indicates the deposit has a number of favourable mining
    characteristics.
    The key findings from the model are:
    • Low average strip ratio of 0.51.
    • High conversion rate with 96% of the resource falling within the optimised pit
    shell
    • No pre-stripping is required.
    The Scoping Study makes the following comment in relation to the ore grade and
    impurities:
    • By international standards the iron ore grade is lower than typical for direct
    shipped ores and the impurity levels are higher than desired. However, this
    appears to be more a disadvantage than a project impediment. The ore may be
    amenable to upgrading by blending, selective mining or beneficiation during
    processing.
    “The Mayoko Iron Ore project is proving to be a low cost DSO deposit with robust
    economics and a very real path to production. Given the low risk jurisdiction,
    supportive government and infrastructure largely in place, DMC’s intention is to bring
    the project into production as quickly as possible” Executive Director David Sumich
    said.
    DMC confirms that, effective immediately, it is commencing a pre-feasibility
    assessment of the Mayoko Iron Ore Project which includes further drilling (scheduled to
    start August 2008), metallurgical studies and also the necessary government
    agreements and regulatory approvals.
    For further information please contact:
    David Sumich, Executive Director, DMC Mining Limited: +61 8 9486 1909
    Dean Richardson. Investor Relations Manager, DMC Mining Limited : +61 8 9486 1909
    James Moses, Partner, Fortbridge Consulting: +61 420 991 574
    Competent Persons: The contents of this report relating to geology and the exploration targets and results
    are based on information compiled by William Witham, a Member of the Australian Institute of Geoscientists.
    He has sufficient experience related to the activity being undertaken to qualify as a “Competent Person”, as
    defined in the 2004 edition of the Australasian Code for Reporting of Exploration Results. William Witham also
    has sufficient experience relevant to the styles of mineralisation and types of deposit under consideration. He
    consents to the inclusion in this report of the matters compiled by him in the form and context in which they
    appear.
    Mayoko Iron Ore Project
    Scoping Study
    June 2008
    Mayoko Iron Ore Project
    Scoping Study
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    Disclaimer
    This Scoping Study (Report) has been prepared for DMC Mining Limited (DMC Mining) by
    GRD Minproc Limited (GRD Minproc), based on assumptions as identified throughout the text and
    upon information and data supplied by others.
    The Report is to be read in the context of the methodology, procedures and techniques used,
    GRD Minproc's assumptions, and the circumstances and constraints under which the Report was
    written. The Report is to be read as a whole, and sections or parts thereof should therefore not be
    read or relied upon out of context.
    GRD Minproc has, in preparing the Report, followed methodology and procedures, and exercised due
    care consistent with the intended level of accuracy, using its professional judgment and reasonable
    care. However, no warranty should be implied as to the accuracy of estimates or other values and all
    estimates and other values are only valid as at the date of the Report and will vary thereafter.
    Parts of the Report have been prepared or arranged by DMC Mining or third party contributors, as
    detailed in the document. While the contents of those parts have been generally reviewed by
    GRD Minproc for inclusion into the Report, they have not been fully audited or sought to be verified by
    GRD Minproc. GRD Minproc is not in a position to, and does not, verify the accuracy or completeness
    of, or adopt as its own, the information and data supplied by others and disclaims all liability, damages
    or loss with respect to such information and data.
    In respect of all parts of the Report, whether or not prepared by GRD Minproc, no express or implied
    representation or warranty is made by GRD Minproc or by any person acting for and/or on behalf of
    GRD Minproc to any third party that the contents of the Report are verified, accurate, suitably qualified,
    reasonable or free from errors, omissions or other defects of any kind or nature. Third parties who rely
    upon the Report do so at their own risk and GRD Minproc disclaims all liability, damages or loss with
    respect to such reliance.
    GRD Minproc disclaims any liability, damage and loss to DMC Mining and to third parties in respect of
    the publication, reference, quoting or distribution of the Report or any of its contents to and reliance
    thereon by any third party.
    This disclaimer must accompany every copy of this Report, which is an integral document and must be
    read in its entirety.
    Mayoko Iron Ore Project
    Scoping Study
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    Table of Contents
    Disclaimer...................................................................................................................... i
    1. EXECUTIVE SUMMARY .......................................................................................... 1
    1.1 SCOPE OF WORK .............................................................................................................................1
    1.2 RECOMMENDATIONS......................................................................................................................2
    1.3 KEY REQUIREMENTS TO ADVANCE ..............................................................................................3
    1.4 PEER REVIEW ..................................................................................................................................3
    1.5 HAEMATITE ORE RESOURCE .........................................................................................................4
    1.6 MINE MODELLING............................................................................................................................6
    1.7 PROCESSING OPTIONS...................................................................................................................6
    1.7.1 Haematite Plant ...................................................................................................................6
    1.7.2 Magnetite Plant....................................................................................................................7
    1.8 REVENUE PREDICTIONS .................................................................................................................7
    1.9 PROJECT DEVELOPMENT TIMETABLE..........................................................................................8
    1.10 HAEMATITE PLANT CAPITAL EXPENDITURE ................................................................................9
    1.11 HAEMATITE PLANT OPERATING COST ESTIMATE ....................................................................12
    1.12 INFRASTRUCTURE .........................................................................................................................12
    1.12.1 Rail....................................................................................................................................13
    1.12.2 Port Facilities .....................................................................................................................14
    1.13 SOVEREIGN RISK ...........................................................................................................................16
    APPENDIX A HAEMATITE PLANT FLOWSHEET............................................................ 17
    APPENDIX B HAEMATITE PLANT GENERAL ARRANGEMENT DRAWING .................... 18
    APPENDIX C HAEMATITE PLANT ELEVATION AND SECTION DRAWING .................... 19
    REFERENCES .................................................................................................................... 20
    Mayoko Iron Ore Project
    Scoping Study
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    1. EXECUTIVE SUMMARY
    DMC Mining Limited (“DMC Mining”) Mayoko Iron Ore Project is still in its infancy. The exploration
    lease was obtained barely 6 months ago in December 2007 and the sole drilling program was
    performed in approximately 1975. Since this time the lease has been dormant. Regardless of this, in
    the current market the project has a surprisingly high number of positive attributes despite the lack of
    attention and the short time that DMC Mining has had to advance the project.
    The project is located in the Republic of the Congo approximately 300 km northeast of Point Noire.
    DMC Mining reports that the project contains a 750 to 800 Mt magnetite exploration target1 that is
    overlaid with a 33 Mt haematite deposit that is open along strike and at depth.2 Geological modelling
    has outlined a haematite exploration target of 110 to 135 Mt.3
    This report by GRD Minproc Limited (“GRD Minproc”) assesses at a scoping study level the option of
    treating the ore body using a staged approach. Stage 1 would see the construction of a crushing and
    screening plant to process haematite and produce direct-shipped-ore (DSO). The production rate in
    Stage 1A will be 3 Mt/a. This will be ramped up to 11 Mt/a within approximately 2 years in Stage 1B.
    The final stage, Stage 2, will treat magnetite to produce 3 Mt/a of pellets. The processing and
    infrastructure requirements for the haematite and magnetite plants were examined. The mining
    assessment was limited to the Stage 1B, 11 Mt/a haematite plant operation.
    Three of the four key criteria required to bring the haematite plant into production were rated as positive
    while the fourth was given a neutral rating. The sovereign risk, schedule and the capital and operating
    costs were rated positively. The ore body received a neutral rating.
    1.1 SCOPE OF WORK
    DMC Mining requested GRD Minproc complete a scoping study to determine processing options for the
    proposed Mayoko Iron Ore Project. The initial scope of work was to determine likely mining, processing
    and infrastructure requirements to produce 5 Mt/a of haematite at a scoping study level under a directshipped-
    ore scenario.
    The scope of work was expanded part way through the study as it became clear from investigations of
    the infrastructure; (power; rail and port) that these facilities were largely in place. These assets provided
    a potential opportunity to commence operations in a shorter time and at higher production rates than
    originally envisaged. The final scope of work was for an 11 Mt/a haematite plant in Stage 1 with a
    3 Mt/a magnetite plant following in Stage 2.
    While this study does not meet Pre-feasibility Study standards it exceeds Scoping Study requirements
    with a number of key issues examined in considerably more detail than warranted for a Scoping Study.
    In excess of 1500 man-hours were expended across mining, processing and infrastructure
    assessments. This included visits to the Republic of the Congo for discussions with the port, rail and
    power authorities.
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    The final scope of work included:
    • An assessment of mining and processing options to produce nominally 3 Mt/a of pellets from the
    magnetite resource and 11 Mt/a of direct-shipped-ore (lump plus fines) from the haematite
    resource. Haematite production would commence at 3 Mt/a and be ramped up to 11 Mt/a
    • Assessment of the suitability of the existing rail network for shipment of ore to the port and
    consumables and equipment to the mine site.
    • Assessment of the port facilities including loading options, capacity and maximum ship size and
    turnaround times.
    • Assessment of electrical power availability and supply.
    • Marketing (brief assessment of market conditions and key revenue drivers supplied under separate
    cover).
    • Processing Plant Capital Cost Estimate to +/- 30%.
    • Processing Plant Operating Cost Estimate to +/- 30%.
    • Preliminary Process Flow Diagrams.
    • Preliminary equipment layout and elevations (assuming flat ground with no spatial constraints).
    • Preliminary mine plan including estimated operating and capital costs
    • Preliminary estimates of mine site infrastructure requirements including indicative capital costs of
    access roads, mine and plant site office buildings, workshops and warehouses, accommodation
    camp, communications systems and mobile equipment.
    • Project Development Timetable (Estimated time into production including drilling programs, test
    work, feasibility studies, equipment lead time, construction and engineering durations).
    1.2 RECOMMENDATIONS
    Although the project is at a very early stage of development it appears promising and should be taken
    to a pre-feasibility study level. The economics appear robust and it compares favourably with its peers
    in the mid-west region of Western Australia. The existence of an operating rail line within 3-5 km of the
    proposed mine site raises the possibility of bringing the mine into production within a short time frame.
    The haematite cap appears to be sufficiently large to allow a staged approach to be adopted. Under this
    scenario a relatively low cost beneficiation plant would be built during Stage 1 to process the haematite
    cap. As the rail infrastructure to transport the ore to port is substantially in place processing rates of up
    to 3 Mt/a could be comfortably accommodated at start-up. This could then be ramped up to 11 Mt/a
    when the rail spur line and wharf facilities to the north of Pointe Noire are complete. This approach
    would fully utilise the installed equipment, supply early cash flow and provide a rapid payback on the
    initial capital cost of the processing plant. Stage 2 would see the development of a magnetite plant.
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    1.3 KEY REQUIREMENTS TO ADVANCE
    The key requirements to advance the project to the next stage are:
    • Geological resource definition for both the haematite and magnetite
    • Metallurgical test work covering ore types and spatial location within the ore body
    • Marketing information on the minimum product specifications required for sale
    • Detailed examination of rail and port requirements
    • Agreements from the rail and port authorities for shipping ore
    1.4 PEER REVIEW
    Although the Mayoko Iron Ore Project is at a very early stage of development the preliminary
    economics appear attractive and therefore justify advancing to a more detailed level of assessment. In
    terms of development it is probably fair to compare the project with operators in the mid-west region of
    Western Australia. These all have relatively young projects and operate, or are contemplating
    operating, far smaller ventures than the major suppliers, BHP Billiton and Rio Tinto who operate in the
    Pilbara region.
    It is beyond the scope of this report to conduct a full analysis of DMC Mining’s peers in the mid-west
    region. However, a cursory analysis indicates DMC Mining’s Mayoko Iron Ore Project compares
    favourably. Whilst there is a sovereign risk that does not exist for junior operators in the mid-west region
    the size of the deposit is comparable and the infrastructure requirements are considerably lower.
    Whilst a sovereign risk does exist, it is relatively low. The existence of an operating rail line within 5 km
    of the proposed mine site that runs directly to the port at Pointe Noire further enhances the project. This
    reduces the initial capital cost and provides the opportunity to bring the project online in a shorter time
    frame and at higher production rates. In contrast, the production for the mid-west iron ore producers is
    limited until such time that new rail lines and the new port at Oakajee are constructed.
    All the mid-west operators started, or proposed to start operations with:
    • Small initial haematite deposits, typically 5 to 15 Mt.
    • Low production rates, typically 1 to 2 Mt/a at start-up.
    • Long transport distances using either road haulage with distances in excess of 220 km and up to
    380 km or road and rail with road haulage in excess of 65 km followed by rail haulage in excess of
    100 km.
    • Three of the operators (Gindablie Metals Ltd, Mount Gibson Iron Limited and Midwest Corporation
    Limited) have magnetite projects that were expected to be bought on line in Stage 2 after
    completion of the Stage 1 haematite project. (Note: To raise capital and concentrate on their
    second haematite project Mount Gibson has now divested itself of the magnetite project).
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    In comparison DMC Mining’s Mayoko Iron Ore Project has the following attributes:
    • A 33 Mt initial haematite deposit.
    • The haematite ore body is open along strike and at depth with an exploration target of 110 to
    135 Mt.
    • Higher initial production rates of up to 11 Mt/a.
    • A rail line within 5 km of the mine that goes directly to the port. Total haulage distance is
    approximately 360 km.
    • A large magnetite resource that can be bought on line in Stage 2 after the Stage 1 haematite
    project is completed.
    1.5 HAEMATITE ORE RESOURCE
    By international standards the iron ore grade is lower than typical for direct shipped ores and the
    impurity levels are higher than desired. However, this appears to be more a disadvantage than a project
    impediment. The ore may be amenable to upgrading by blending, selective mining or beneficiation
    during processing. The resource was modelled by Runge Limited and the estimated inventory for 33 Mt
    haematite deposit is shown in Table 1.1. Under the JORC code the resource is classified as inferred.
    The model assigned the ore to one of three domains:
    • Iron Cap
    • In situ
    • Detrital.
    The topography which can be seen in Figure 1.2 indicates the terrain is hilly with the deposit forming a
    ridge which rises from the countryside to the east. The iron cap ore type is the uppermost layer and
    covers the deposit. The in situ ore type lies below the iron cap. The detrital ore mainly occurs on the
    edges of the deposit.
    Table 1.1
    Resource Inventory at 50% Fe Cut-Off
    Domain Volume m3 Tonnes Fe % Al2O3 % SiO2 % P %
    Iron Cap 380 000 1 330 000 62.17 1.10 5.93 0.09
    In Situ 5 171 250 16 098 500 55.56 3.04 11.71 0.10
    Detrital 5 587 500 15 645 000 54.90 4.91 9.45 0.09
    Total / Average 11 138 750 33 073 500 55.51 3.85 10.41 0.09
    Geological mapping indicates the resource potentially contains 110 to 135 million tonnes. The historical
    drilling covered an area of approximately 5 km along strike and 1.2 km across strike with the greatest
    density of holes covering an area of approximately 1.4 km x 400 m. All holes intercepted iron
    mineralisation and 36 of the 38 holes (95%) ended in mineralised zones with grades in excess of 50%
    iron and are therefore open.2
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    The Mayoko Iron Ore Project deposit is contained within the “Massif du Chaillu” formation. This
    formation runs along a roughly north – south axis. It commences in the Republic of the Congo in the
    south and extends into Cameroon in the north. The Massif du Chaillu formation hosts multiple iron ore
    deposits with a combined estimated resource in excess of 2.5 billion tonnes. Including Mayoko, seven
    of the deposits are estimated to contain more than 100 Mt of iron ore.4,5,6 The nearest deposit, Zanaga,
    is approximately 100 km east in the Republic of the Congo and the furthest deposit, Mbalam, is
    approximately 550 km north in the Cameroon.
    Figure 1.1
    Known Iron Ore Deposits within the Massif du Chaillu Formation
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    1.6 MINE MODELLING
    Geological mapping indicates the resource potentially contains 110 to 135 Mt. However, the mine plan
    relates to the 33 Mt inferred resource. The preliminary mine design modelling based on a 55% Fe runof-
    mine product and 50% Fe cut-off grade indicates the deposit has a number of favourable mining
    characteristics. The key findings from the model are:
    • Low average strip ratio of 0.51.
    • High conversion rate with 96% of the resource falling within the optimised pit shell
    • No pre-stripping is required.
    Insufficient information is available at present to determine the ultimate tonnage, grade and quality of
    the deposit. Nevertheless, with favourable mine characteristics other options such as selective mining
    may be possible that provide alternatives to selling a low grade product. Selective mining would
    increase the mining costs by a small amount but would result in a higher grade product which would
    attract a higher sale price. To allow for the possibility to upgrade the ore in the future the estimated
    mining costs for the 33 Mt haematite deposit has been increased from US$ 4.50 to US$ 6.00 per tonne.
    This would allow for blending ore from the further reaches of the deposit or selective mining with more
    material sent to waste. Trade off studies will be conducted at a later date when more information about
    the deposit is known. These studies will examine the relative merits of selling the product as is,
    blending, selective mining and addition of extra equipment in the process plant to reject impurities.
    This type of reallocation would not affect the other positive attributes of the ore body. No pre-stripping is
    required. During the first few months when the 30 m deep iron cap is processed no waste is generated.
    The mine plan indicates that the top 70 m, from 820RL to 750RL, would be mined completely. This
    material would be directed to the processing plant or to the waste dumps. The top 70 m has a strip ratio
    of approximately 0.36 and contains approximately 5.5 Mt of waste and 15 Mt of ore. From 750 RL down
    selective mining would be used with the waste left in the pit.
    At this time the ore resource has been rated as neutral. The lower than desired iron grades are offset
    by the fact that the host geology is favourable; the resource is open at depth and along strike; the
    mining costs for the 33 Mt haematite deposit are low and the majority of the resource can be mined and
    processed.
    1.7 PROCESSING OPTIONS
    1.7.1 Haematite Plant
    The resource consists of a haematite cap overlaying a magnetite deposit. The haematite cap must be
    mined first to access the magnetite. Several options were examined to determine the best choice of
    processing route and equipment. The criteria employed to assess the options were:
    • The capacity of the haematite plant using a somewhat conservative design principle had to match
    the maximum carrying capacity of the rail system as it exists at present.
    • As far as possible the equipment selected for the haematite plant had to be suitable for use in the
    later magnetite plant.
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    • To minimise financing costs the design was to allow for staged construction such that production
    could commence sooner at lower throughput rates and build up to full production by installation of
    additional modules.
    To model the circuit and size equipment a number of assumptions were made regarding the ore
    characteristics. The haematite ore was assumed to have similar characteristics to ore from the Pilbara
    region of Western Australia. When compared with ore from the mid-west region the Pilbara ore is
    typically more friable and produces more fine than lump ore. The higher fines production from the
    Pilbara ores reduces revenue as lump ore commands a premium to fines but on a like for like basis the
    ore can be processed at higher capacity rates than the mid-west ores as it is more friable.
    This study proposes treating the haematite in a conventional two stage crushing circuit to generate two
    products, lump and fines. The nominal size range of lump ore is larger than 6.3 mm but smaller than
    31.5 mm. The fine product is nominally all ore that is less than 6.3 mm in size. As a general philosophy
    the equipment selection and plant layout has been based on the following principles:
    • All equipment selected is robust and suitable for heavy duty. This type of equipment is more
    expensive but is capable of treating harder ores.
    • The circuit design has assumed a long mine life and consequently the equipment and layout has
    been chosen to minimise the operating and maintenance costs. This adds to the initial capital
    costs.
    The process flow sheet, general arrangement drawing and elevation and section drawing for the
    haematite plant are attached in the Appendices at the end of this report.
    1.7.2 Magnetite Plant
    The magnetite plant provides the operation with longevity. The processing and infrastructure
    requirements were assessed to determine what additional equipment and infrastructure would be
    required to produce pellets and how well these requirements fitted with the haematite plant. The
    assessment concluded the required mills, magnetic separators and pelletising plant will be a natural
    add-on in later years. However, the emphasis of the current study is on developing the haematite.
    Development of the magnetite will follow one step behind and will be examined in greater detail in later
    studies.
    1.8 REVENUE PREDICTIONS
    It is beyond the scope of this report and the expertise of the authors to predict what price the various
    iron ore products (fines, lump and pellets) could command in the future. There are a multitude of
    opinions and analysis’s available in the public domain on iron ore pricing that the reader can refer to.
    Nevertheless, in order to calculate revenue for the Mayoko Iron Ore Project, low and high sale prices
    for fines, lump and pellets have been chosen. The calculated revenue is shown in Table 1.2. It should
    be noted that these calculations do not constitute predictions. They are included to provide an indication
    of the potential revenue stream.
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    Table 1.2
    Mayoko Revenue Projections at Various Iron Ore Prices
    Current Spot Price Long term high estimate Long term low estimate
    Production
    t/a
    Grade
    % Fe
    Sale Price
    US$/ t Fe
    Revenue
    US$ M/yr
    Sale Price
    US$/ t Fe
    Revenue
    US$ M/yr
    Sale Price
    US$/ t Fe
    Revenue
    US$ M/yr
    Haematite
    Lump 4,950,000 56% 180.00 $499.0 56.25 $155.9 31.05 $86.1
    Fines 6,050,000 56% 180.00 $609.8 45.00 $152.5 27.00 $91.5
    Total 11,000,000 $1,108.8 $308.4 $177.5
    Haematite
    Lump 1,350,000 56% 180.00 $136.1 56.25 $42.5 31.05 $23.5
    Fines 1,650,000 56% 180.00 $166.3 45.00 $41.6 27.00 $24.9
    Total 3,000,000 $302.4 $84.1 $48.4
    Magnetite
    Pellets 3,000,000 67% 180.00 $361.8 74.25 $149.2 37.80 $76.0
    The basis for the prices chosen including the premium attributed to lump and pellets is:
    • The iron content for the haematite is low and as a consequence the realised sale price has been
    discounted.
    • The low revenue estimate is based on fines fetching $US27 per dry tonne of contained iron in
    today’s dollar terms. This is at the low end of prices realised from 1980 to 2004 and provides a
    reasonable estimate of the minimum revenue stream that could be realised. It is assumed that if
    prices are low, that the economy is in a downturn and the premium for lump and pellets will be
    lower. A 15% premium for lump and a 40% premium for pellets relative to fines have been used in
    the calculations.
    • The high revenue estimate is based on fines fetching $US45 per dry tonne of contained iron in
    today’s dollar terms. This assumes demand from China and India will remain high for the medium
    term but still assumes a discount for the low iron content. In line with higher demand, higher
    premiums for lump and pellets have been assumed. A 25% premium for lump and a 65% premium
    for pellets relative to fines have been used in the calculations.
    • Typical physical characteristics for iron ore from the Pilbara region in Western Australia have been
    assumed when assigning lump to fines ratios for the purpose of calculating revenue. Any changes
    to this ratio will affect the revenue. The ores from the Western Australia mid west region have a
    higher lump to fines ratio. Some of these ores produce approximately twice as much lump as fines
    with ratios up to 67:33.7
    1.9 PROJECT DEVELOPMENT TIMETABLE
    The proposed project schedule of first operation of 11 Mt/a commencing within 4 years is heavily reliant
    on a streamlined progression from this Scoping Study through Pre-feasibility and Definitive (Bankable)
    Feasibility Studies, then into construction and commissioning. The project development schedule has
    placed the priority on the haematite plant development. The magnetite development is scheduled to run
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    one step behind to ensure the project management resources are concentrated on expediting the
    design, engineering, procurement, construction and commissioning of the haematite plant. Continuity
    and flow of information from the study phases through design and into construction will allow production
    to commence as soon as possible.
    The magnetite plant has a number of long lead items such as the mills and the pelletising plant. The
    subordinate development of the magnetite plant design will allow adequate time for this equipment to
    be correctly specified, procured and expedited.
    1.10 HAEMATITE PLANT CAPITAL EXPENDITURE
    The estimated total capital expenditure for the 11 Mt/a Stage 1B haematite plant is US$ 486 M. This
    includes US$428 M for direct and indirect costs and an additional US$ 58 M in provisional costs. The
    direct and indirect costs include a contingency provision and are judged to have an accuracy of ±30%.
    The direct and indirect cost estimate covers the areas and facilities as outlined in the scope of work and
    discussed in this report. This includes the following;
    • Process plant including train load out facilities and rail loading loop;
    • Mining fleet and mine facilities;
    • Mayoko site infrastructure such as the accommodation village and airfield.
    • Pointe Noire port facilities excluding rail spur line & wharf;
    • Rail rolling stock (locomotives and wagons);
    • First fill consumables and spares and
    • Engineering, procurement and construction management (EPCM) costs.
    No allowances were made in the capital estimate for:
    • Earthworks other than initial site preparation (grubbing & clearing);
    • Additional allowance for any seismic activity;
    • Environmental controls;
    • Capital required to sustain the operation over the anticipated mine life;
    • Cost associated with obtaining regulatory approvals and
    • Owners cost
    An additional US$ 58 M in provisional costs has been allowed to cover the following:
    • Spur line from main Point Noire-Brazzaville line to the new wharf;
    • Wharf;
    • Repairs and modifications to the existing rail line and
    • Regional roads around the new spur line and to the new wharf
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    The estimate for the regional roads and repairs and modifications to the existing rail line is an allowance
    only. At this stage the line has not been inspected along its full length from Pointe Noire to Mayoko.
    However, it is currently used for passenger and freight services and was used previously to transport
    ore. As a consequence major repairs are not expected.
    The cost of the spur line is judged to have an accuracy of +/- 30% but this is heavily qualified as the
    route and ground conditions have not been verified. The spur line costs are based on the assumptions
    that; the route is reasonably direct; the terrain is relatively flat; ground conditions are stable; minimal
    road and pedestrian crossings are required and security fencing is only required along part of the line.
    The initial indications are that these assumptions are reasonable but until the route can be verified and
    right of access approvals granted the costs are considered provisional only.
    The cost of the wharf is judged to have an accuracy of +/- 30% but this is heavily qualified as no
    bathometry (sea depth) and sea bed data has been sighted. The wharf costs are based on the
    assumptions that; the transition from land to sea is simple with stockpiles in close proximity to the
    waters edge; the sea bed is stable; no dredging is required; minimal navigation and berthing aids are
    required and a finger style wharf of 350m total length is sufficient. The initial indications are that these
    assumptions are reasonable but until more information is available the costs are considered provisional
    only.
    Commencing operations with a 3 Mt/a plant, leasing locomotives and using contract mining allows in
    excess of US$285 M of capital expenditure to be deferred. The total capital expenditure of US$ 198 M
    includes US$192 M for direct and indirect costs and an additional US$ 6 M in provisional costs. This
    smaller scale start-up operation is dependent on the Pointe Noire Port Authority granting temporary
    access to the existing port.
    The estimated capital expenditure for the 11 Mt/a and the 3 Mt/a plant are shown in 3. All costs are
    estimated in US dollars as at the second quarter 2008.
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    Table 1.3
    Haematite Plant Capital Expenditure Estimate
    Haematite
    Stage 1B
    11 Mt/a
    US$ M
    Haematite
    Stage 1A
    3 Mt/a
    US$ M
    Mining
    Mine Facilities 6.6 6.6
    ROM Stockpile 2.3 2.3
    Mining Fleet 42.2 0.0 Contract mining for 3 Mt/a
    Total Mining 51.1 8.9
    Process Plant
    Primary Crushing 17.5 17.5
    Secondary Crushing & Screening 17.3 17.3
    Train Load Out & Plant Rail Loop 33.6 18.6 Load out by FEL for 3 Mt/a
    Plant Infrastructure 32.2 22.2
    Total Process Plant 100.6 75.6
    Mayoko Area Infrastructure 9.0 9.0
    Pointe Noire Area
    Port area infrastructure 15.7 15.7
    Wagons and locomotives 111.1 18.2 Lease loco's & 1/3 rd wagons req'd for
    3M t/a
    Wagon dumper & ship loader 28.8 14.4
    Buildings (maintenace workshop, admin, storage shed) 26.5 13.2
    Total Pointe Noire Area 182.1 61.5
    Miscellaneous (reagents, spares, commissioning) 10.6 6.4
    Total Direct Cost 353.4 161.4
    Indirect Costs (Engineering & Construction Management) 74.3 30.1
    TOTAL DIRECT & INDIRECT COSTS 428 192
    Provisional Costs
    Spur line to Point Noire wharf 28.5 0 Spur line not req'd for 3 Mt/a
    Wharf 23.9 0 Wharf not req'd for 3 Mt/a
    Repairs and modifications to existing line 5 5
    Regional roads at new wharf 1 1
    Total Provisional Costs 58 6
    TOTAL COST 486 198
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    1.11 HAEMATITE PLANT OPERATING COST ESTIMATE
    The estimated operating costs are based on processing 11 Mt/a of ore to produce direct-shipped lump
    and fine products. All costs are estimated in US dollars as at the second quarter 2008 and are judged to
    have an accuracy of ±30%. The operating cost estimate is summarised in Table 1.4
    Table 1.4
    Haematite Plant Operating Costs
    US$ / t crushed Total US$ / yr
    Mining
    Mine production 4.50 49,500,000
    Blending / selective mining allowance 1.50 16,500,000
    Total Mining 6.00
    Process Plant
    Labour 0.23 2,480,000
    Power 0.27 2,952,000
    Consumables 0.06 658,000
    Maintenance 0.77 8,483,000
    Administration 0.03 330,000
    Total Process Plant 1.35
    Product Transport 14.40 158,400,000
    Export Charges (port & royalties) 0.50 5,500,000
    TOTAL OPERATING COST 22.25 244,803,000
    The operating costs for the 3 Mt/a start-up facility have not been estimated. A small rise in costs can be
    expected as fixed costs will be spread across 3 Mt/a production instead of 11 Mt/a. Additional costs
    beyond this resulting from contract mining, locomotive lease and the port authority lease and right of
    access costs will also need to be absorbed.
    1.12 INFRASTRUCTURE
    The existence of a rail line from the port at Pointe Noire to Mbinda on the Gabon border in the north that
    passes within 5 km of the proposed plant location provides considerable leverage to reduce the project
    costs. It provides a ready made transport corridor to move equipment and supplies from the port to site
    and iron ore from the site to port for export.
    An airfield capable of handling light planes exists within close proximity to the mine site. The airstrip
    needs some upgrading but once this is done it will be capable of moving personnel from Pointe Noire to
    site. Pointe Noire is well serviced with regular flights from Europe and South Africa.
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    The port facilities are capable of handling containerised and break bulk goods. The facilities are
    sufficiently modern and have adequate capacity to handle all plant and construction equipment that
    may be required.
    Additional detail on the available infrastructure is discussed below along with comments on possible
    modification and/or upgrade requirements.
    1.12.1 Rail
    The ROC has an existing rail system, the Chemin de Fer Congo-Ocean (CFCO). This is operated and
    maintained by the Federal Government. Two lines are installed and operating. The main line comprises
    a dual track running east-west from the capital city, Brazzaville, in the south east to the second largest
    city, Pointe Noire, on the west coast. This is a major corridor for moving freight and passengers
    between the two major cities.
    The second line comprises a single track running from Mbinda on the Gabon border in the north to the
    town of Dolisie in the south where it connects into the Brazzaville-Pointe Noire line. This line was
    constructed to service a manganese mine operated by Comilog in Gabon from 1962 to 1986. Comilog
    transported manganese ore to the port for export. The northern line runs past the town of Mayoko with
    DMC Mining’s ore body within 5 km of the line. The close proximity of the rail line, town and ore
    resource is shown in Figure 1.2.
    The manganese company has ceased business but the line remains operational with a weekly
    passenger service using the facilities. The rail authority has indicated that the line is available for use by
    DMC Mining to transport iron ore. The initial evaluation indicates the line is capable of carrying 11 Mt/a.
    The CFCO rail system is narrow gauge of 1067 mm (3’6”). This gauge is commonly used in Central and
    West Africa, Europe and Australasian countries. The Brazzaville-Point Noire rail uses a 46 kg/m rail
    (high strength) which is suitable for industrial freight. There are two sections to the northern (Mayoko)
    line. The first shorter section from Dolisie to Mossendjo uses 36 kg/m rail section (medium strength).
    The second and longer section extends from Mossendjo to Gabon. This section was constructed by
    Comilog for heavy haulage and utilises 50 kg/m rail (high strength).
    The rail system is well suited for the exploration and construction phases of the project. It can be used
    “as is” with no modifications for these stages of the project. The CFCO can supply transportation
    services for the mobilisation of exploration equipment and supplies to site, using their existing diesel
    locomotives and freight wagons. During construction the CFCO can facilitate the transportation of
    break-bulk and containerised equipment, fabricated structure sections and consumables.
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    Figure 1.2
    Rail Line at Mayoko
    Extensions to the rail line are required for the production phase. A rail loop of approximately 5 km will
    be built for the 3 M t/a start-up during Stage 1A construction. This will link into the northern rail line in
    the vicinity of Mayoko and extend to the processing plant. A front-end-loader will be used to load the
    ore wagons at the processing plant. The ore will be transported to the existing port where it will be
    unloaded and stockpiled using temporary facilities prior to loading onto ships.
    During the Stage 1B upgrade which will increase production to 11 Mt/a, automated load out facilities will
    be constructed at site. The spur line, wharf and permanent stockpiles, wagon unloading, ship loading
    and associated facilities at Pointe Noire will also be built during this stage.
    1.12.2 Port Facilities
    The port facilities are approaching the limit of their capacity and shipping 11 Mt/a through the existing
    port facilities is not feasible. New facilities which would include a wharf and spur line from the existing
    rail line are needed. The port authorities have indicated a site approximately 10 km north of the port is
    available.
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    For the proposed 11 Mt/a production of haematite lump and fines product a “Capesize” vessel
    (approximately 175 000 t to 250,000 t capacity) is preferred. It is possible to move this amount of ore
    with a smaller vessel such as a 65,000 tonne “Panamax” but this would require a very tightly controlled
    shipping schedule with average turnaround times of 2.2 days. This schedule would negate redundancy
    within the port system.
    The existing port facilities can not accommodate “Capesize” vessels as these require an 18 m minimum
    draft. The maximum draft the port can currently accept is 13 m, which is adequate for a “Panamax” size
    ship. As a result the project will look at a new jetty, ship loading and stockyard facility. The proposed
    location is north of Pointe Noire in the existing industrial zone area near the oil refinery and can be seen
    in Figure 1.3
    The estimated 15 km spur line and new wharf facility will increase the capital cost significantly and
    increase the project duration. However, during discussions with the port authorities in May 2008 they
    indicated they were willing to consider a two stage approach. Under this scenario temporary facilities
    would be installed in the port to export approximately 3 Mt/a. To export 3 Mt/a can be accomplished
    using “Panamax” size ships with an average turn around time of 8 days. This is within the capabilities of
    the existing port facilities. The temporary installation would be used for approximately 2 years while the
    new spur line and wharf were built. When the new facilities were complete, production would be ramped
    up to 11 Mt/a. Negotiations have commenced with the port authorities to bring the operation into
    production in two stages.
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    Figure 1.3
    Pointe Noire Port Facilities
    Map Courtesy of GoogleEarth®
    1.13 SOVEREIGN RISK
    The current government headed by Denis Sassou-Nguesso has been in power for over 10 years and
    appears stable. The specialist risk consultancy firm, Control Risks, has rated the Republic of the Congo
    as one of the lowest risk countries in Africa based on both security and political risk.8 Foreign
    investment seems to be encouraged. Magindustries has just committed to construction of a US$723 M
    potash plant with construction planned to commence in Q3, 2008.9 In May 2007 Mining Projects
    Development (MPD) signed agreements with the government and is ramping up the drilling program
    and concurrent studies for the Zanaga iron ore deposit 100 km east of the Mayoko deposit.10 The
    Congo electrical authority has committed to bringing a 25 MW power plant on-line by the end of this
    year with a 400 MW plant scheduled to be on-line by the end of 2010.11
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    APPENDIX A HAEMATITE PLANT FLOWSHEET

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    APPENDIX B HAEMATITE PLANT GENERAL ARRANGEMENT DRAWING
    A
    60024 18.03.08 60024-0012-05-121-001 A
    JNM
    JNM
    1 : 1000 DMC MINING LTD
    MAYOKO IRON ORE PROJECT
    HEMITITE PLANT
    GENERAL ARRANGEMENT
    0
    20
    40 80 120 160 200m
    100000 200000 130000
    C
    C
    ROM PAD.
    BASED ON CAT 989
    HAUL TRUCK.
    PROPOSED RAIL LOOP.
    BN-202 .
    FINE ORE TRAIN
    LOAD OUT BIN.
    (1000m)
    ST-202
    FINE ORE STOCKPILE.
    (80000m)
    TU-202
    BN-201 .
    LUMP ORE TRAIN
    LOAD OUT BIN.
    (1000m)
    TU-201
    C
    C
    BL-003 BL-001
    CR-001
    CONVEYOR CV-005.
    FINES TRANSFER.
    CONVEYOR CV-006.
    FINES TRANSFER.
    C
    C
    SC-002
    PRIMARY SCREEN
    No.2
    SC-001
    PRIMARY SCREEN
    No.1
    LUMP STACKER
    CV-004
    BN-002.
    PRIMARY SCREEN BIN.
    (250m)
    ST-201
    LUMP ORE
    STOCKPILE.
    (80000m)
    CV-001
    PRIMARY CRUSHER DISCHARGE CONVEYOR
    B
    0012-05-121-02
    0012-05-121-02
    A
    PLANT GRID NORTH
    BLD-003
    PRIMARY SCREEN
    BUILDING
    BLD-002
    SECONDARY CRUSHER/TRANSFER BUILDING
    CR-002
    SECONDARY CONE CRUSHER.
    BN-003
    SECONDARY CRUSHER BIN
    (100m)
    BLD-001
    PRIMARY CRUSHER BUILDING
    CR-001.
    PRIMARY GYRATORY CRUSHER.
    FE-001.
    PRIMARY CRUSHER APRON FEEDER.
    CV-003
    AREA 011 & 012 CRUSHING AND SCREENING
    FOR INFORMATION
    ONLY
    ISSUED FOR INFORMATION ONLY
    D
    C
    A
    B
    H
    G
    E
    F
    1 2 3 4 5 6 7 8 9 10 11 12
    No. BY DATE REVISION CHECKED APPROV.
    BY DATE CLIENT
    PROJECT No. DRG SIZE REV
    No.
    DRAWING No.
    A1
    PROJECT APPR.
    DESIGN APPR.
    DESIGNED
    CHECKED
    DRAWN
    TITLE
    SCALE
    DRAWING No. REFERENCE DRAWINGS
    CLIENT:
    COPYRIGHT C
    This drawing remains the property of
    GRD MINPROC LIMITED and may not be
    copied in any way without prior written
    approval from this company
    ABN 52 008 992 694
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    Page 19
    APPENDIX C HAEMATITE PLANT ELEVATION AND SECTION DRAWING
    A
    60024 18.03.08 60024-0012-05-121-002 A
    JNM
    JNM
    DMC MINING LTD
    HEMATITE PLANT
    0
    7.5
    15 30 45 60 75m
    SCALE 1:750
    RL:7500
    RL:0.000 DGL
    RL:39500 WP
    RL:0.000 DGL
    RL:15000 TOS
    RL:25200 TOP PAD
    RL:0.000 DGL
    RL:30325 WP
    MAYOKO IRON ORE PROJECT
    1 : 750
    ELEVATIONS AND SECTIONS
    B
    0012-05-121-001
    SECTION
    0012-05-121-001
    SECTION C
    RL:7500
    RL:0.000 DGL
    RL:39500 WP
    RL:20000 TOS
    ROM PAD.
    BASED ON CAT 789
    HAUL TRUCK.
    SC-002.
    PRIMARY SCREEN.
    SC-001.
    PRIMARY SCREEN.
    CONVEYOR CV-006.
    FINES TRANSFER.
    CONVEYOR CV-007.
    FINES TRANSFER.
    RL: 15000 TOS
    300000 130000
    100000 200000
    0012-05-121-001
    A
    0012-05-121-001
    SECTION D
    284994
    
     BN-201
    (1000m)
    RAIL LINE
    TU-201
    ST-001
    LUMP ORE
    STOCKPILE.
    (80000m)
     CV-004
    
    7487 6487
    FE-202  FE-201
    BN-003
    4400 38225
     BL-001
    BN-001
    CR-001
    CR-002 
    RL:0.000 DGL
    REINFORCED
    ROM WALL
     CR-001
    CV-001
    CR-001.
    PRIMARY GYRATORY CRUSHER.
    FE-001.
    PRIMARY CRUSHER APRON FEEDER.
    BN-002.
    PRIMARY SCREEN BIN.
    (250m)
    RL:25200 TOP PAD
     CR-001
    ROM PAD
    ST-202
    OMITTED FOR CLARITY
     CV-201
    ST-201
    LUMP ORE
    STOCKPILE.
    (80000m).
    TU-201
    CV-004
    FOR INFORMATION
    ONLY
    AREA 011 & 012 CRUSHING AND SCREENING
    ISSUED FOR INFORMATION ONLY
    SECTION
    D
    C
    A
    B
    H
    G
    E
    F
    1 2 3 4 5 6 7 8 9 10 11 12
    No. BY DATE REVISION CHECKED APPROV.
    BY DATE CLIENT
    PROJECT No. DRG SIZE REV
    No.
    DRAWING No.
    A1
    PROJECT APPR.
    DESIGN APPR.
    DESIGNED
    CHECKED
    DRAWN
    TITLE
    SCALE
    DRAWING No. REFERENCE DRAWINGS
    CLIENT:
    COPYRIGHT C
    This drawing remains the property of
    GRD MINPROC LIMITED and may not be
    copied in any way without prior written
    approval from this company
    ABN 52 008 992 694
    Mayoko Iron Ore Project
    Scoping Study
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    Page 20
    REFERENCES
    1 DMC Mining, ASX Announcement, 3 December 2007
    2 DMC Mining, ASX Announcement, 28 February 2008
    3 DMC Mining, ASX Announcement, 7 May 2008
    4 Personal communications B. Franzen DMC Mining, B.R.G.M Congo Geologie Map, 1963
    5 Congo Metallogenic Map 1:1,000,000
    6 Porter GeoConsultancy Pty Ltd, Ore Deposit Description Database Gabon Iron,
    http://www.portergeo.com.au/database/mineinfo.asp?mineid=mn1211, [Accessed 28 May 08]
    7 Muir A, Rowell A, Tonkin S., Mid-West Iron Ore Book Steeling the Limelight from the Pilbara, August
    2006, Hartleys Ltd
    8 DMC Mining, ASX Announcement, 29 April 2008
    9 http://www.magindustries.com/detail.php?id=510 [accessed 5 June 2008]
    10 L’exploitation du fer dans la Lékoumou augure de bonnes perspectives pour l’économie congolaise,
    http://www.congo-site.com/pub/fr/v4x/actualites/article.php?num=6819 [accessed 29 May 2008]
    11 Meeting 30 April 2008 with Mr Henri Inokmis, Directeur Départemental, Société Nationale d’électricité
 
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