unlocking the value of low grade ultramafic nickel...
TRANSCRIPT
Unlocking the value of low grade
ultramafic nickel deposits November 19, 2014
Johnna Muinonen
1
Disclaimer
Cautionary Statements Concerning Forward-Looking Statements This presentation contains "forward-looking information" including without limitation statements relating to mineral reserve estimates, mineral resource estimates, realization of mineral reserve and resource estimates, capital and operating cost estimates, project and life of mine estimates, construction of the mine and related infrastructure, the timing and amount of future production, costs of production, success of mining operations, ability to obtain permitting by the time targeted, size and ranking of project upon achieving production, economic return estimates and potential upside and alternatives. Readers should not place undue reliance on forward-looking statements. Forward-looking statements involve known and unknown risks, uncertainties and other factors which may cause the actual results, performance or achievements of RNC to be materially different from any future results, performance or achievements expressed or implied by the forward-looking statements. The feasibility study results are estimates only and are based on a number of assumptions, any of which, if incorrect, could materially change the projected outcome. Even with the completion of the feasibility study, there are no assurances that Dumont will be placed into production. Factors that could affect the outcome include, among others: the actual results of development activities; project delays; inability to raise the funds necessary to complete development; general business, economic, competitive, political and social uncertainties; future prices of metals; availability of alternative nickel sources or substitutes; actual nickel recovery; conclusions of economic evaluations; changes in project parameters as plans continue to be refined; accidents, labour disputes and other risks of the mining industry; political instability, terrorism, insurrection or war; delays in obtaining governmental approvals, necessary permitting or in the completion of development or construction activities. The MOU with Tsingshan is non-binding and there is therefore no assurance that the strategic alliance with Tsingshan will result in any transaction or venture with Tsingshan. For a more detailed discussion of such risks and other factors that could cause actual results to differ materially from those expressed or implied by such forward-looking statements, refer to RNC's filings with Canadian securities regulators available on SEDAR at www.sedar.com. Although RNC has attempted to identify important factors that could cause actual actions, events or results to differ materially from those described in forward-looking statements, there may be other factors that cause actions, events or results to differ from those anticipated, estimated or intended. Forward-looking statements contained herein are made as of the date of this presentation and RNC disclaims any obligation to update any forward-looking statements, whether as a result of new information, future events or results or otherwise, except as required by applicable securities laws NI 43-101 Compliance The technical information pertaining to the Dumont project feasibility study in this presentation is based on RNC’s technical report dated July 25, 2013 that describes the results of the Dumont project feasibility study and was prepared in accordance with Canadian regulatory requirements by, or under the supervision of, Paul Staples, P. Eng. of Ausenco Limited, Sébastien Bernier, P.Geo. of SRK Consulting (Canada) Inc. and David A. Warren, Eng. of Snowden Mining Industry Consultants, all of whom are independent Qualified Persons as set out in National Instrument 43-101 Standards of Disclosure for Mineral Projects ("NI 43-101"). The Mineral Resource estimate set out in this presentation was classified according to the CIM Definition Standards for Mineral Resources and Mineral Reserves (November 2010) by Sébastien Bernier, P. Geo (OGQ#1034, APGO#1847), Principal Consultant – Resource Geology at SRK. The Mineral Reserve estimate set out in this presentation was classified according to the CIM Definition Standards for Mineral Resources and Mineral Reserves (November 2010) by David A. Warren (OIQ 121481), Principal Consultant – Mining at Snowden. All other technical information in this presentation has been prepared by or under the supervision of Alger St-Jean, P. Geo., Vice President, Exploration of RNC and Johnna Muinonen P. Eng., Vice President, Operations of RNC, each a Qualified Person as defined in NI 43-101. The full Dumont feasibility study, prepared as an NI 43-101 compliant technical report, is available under RNC’s profile on SEDAR at www.sedar.com.
All currency references in U.S. dollars, unless otherwise stated.
www.royalnickel.com
Dumont Project Summary
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Simple flowsheet
Low strip ratio 1.1:1
Competitive electricity costs C$ 4.5 cents/kWh
High grade concentrate – 29% nickel
Non-acid generating waste rock and tailings
All major support infrastructure in place (road, rail, power, water)
Significant communities nearby with long history of resource development
$US 1.1 billion NPV8% at $9.00/lb nickel
1.1 billion tonne reserve at 0.27% nickel
33 year project life
$1.2 billion initial capital investment for 52.5 ktpd mine/mill operation
Dumont Project Location Structural Advantages
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Dumont Site Layout
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TSF 1
TSF 2
Waste
Overburden
Open
Pit
Low Grade
Ore
LGO
OB
LGO
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Dumont Mineralogy Summary
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Recovered nickel minerals
Pentlandite (Fe, Ni)9S8 25-33% Ni
Heazlewoodite Ni3S2 70% Ni
Awaruite Ni3Fe 70% Ni
Other Components
Serpentine (incl. Chrysotile)
Brucite
Magnetite
+/- Olivine
Pyrrhotite - Pyrite
Yields high-grade concentrate
1 cm
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
www.royalnickel.com
Challenge 1: Nickel is contained in recoverable and non-recoverable forms
Challenge 2: Presence of Mg-silicate slimes increase slurry viscosity
Challenge 3: Produce a low cost, robust flowsheet
How do mineral processors address these challenges to reduce risk and understand value?
Characteristics of Low Grade Nickel Ultramafic Deposits
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Challenge 1: Understanding nickel in silicates
Initially in 2008 it was assumed Dumont had fixed nickel in silicates
By late 2010, early 2011 mounting evidence suggested that the fixed nickel assumption was incorrect
Unreconciled assays from mineralogy could not account for nickel head grade in variability samples
Ni flotation recovery was lower than expected in various areas
Realization that RNC needed to understand nickel in silicate variability in the deposit
QEMSCANTM (Quantative Mineralogy)
Electron Microprobe
Metallurgical tests
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Non-domained Rougher Recovery – All Samples
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R² = 0.168
0
25
50
75
100
0 0.2 0.4 0.6 0.8
% N
i R
ou
gh
er
Re
co
ve
ry (
ST
P)
% Ni in STP Sample
R² = 0.2704
0
25
50
75
100
0 0.1 0.2 0.3 0.4 0.5
% N
i R
ou
gh
er
Re
co
ve
ry (
ST
P)
% S in STP Sample
Traditional grade-recovery plots or sulfur-recovery plots cannot indicate recovery
Challenge 1: Nickel in silicates
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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QEMSCAN Results: Variability of Sulphide Mineralogy
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*Defined by EXPLOMINTM Mineralogy
Challenge 1: Nickel in silicates Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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Predicted Recovery by Sulphide Domain
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R² = 0.7135
0
25
50
75
100
0 25 50 75 100% N
i R
ou
gh
er
Re
co
ve
ry (
ST
P)
% Ni Predicted Rougher Recovery
Heazlewoodite Dominant
R² = 0.8024
0
25
50
75
0 20 40 60 80
% N
i R
ou
gh
er R
ec
ove
ry (
ST
P)
% Ni Predicted Rougher Recovery
Mixed Sulphide
Heazlewoodite Dominant Recovery
=18.11+(0.0211*S)+(0.00039*Fe) Mixed Sulphide Predicted Recovery
=9.73+(0.0222*S)+(0.00055*Fe)
Pentlandite dominant group could not be regressed with high R2
Challenge 1: Nickel in silicates Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
www.royalnickel.com
Pn Dominant Domain – Performance Differences?
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Why do high Fe-serpentine samples result in lower recoveries?
Presence of Fe-serpentine indicates increased nickel in silicates
Presence of Fe-serpentine indicates low tenor pentlandite
Challenge 1: Nickel in silicates
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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Frequency distribution for % Ni in Serpentine
Dumont – Electron Microprobe Summary
Challenge 1: Nickel in silicates
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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Metamorphism - Serpentinisation Nickel enrichment of metallic minerals and domaining
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Olivine
Nickel sulphides
Serpentine
Magnetite
Nickel sulphides
Fe-Ni alloy(awaruite)
Dunite Serpentinite
Ni
Challenge 1: Nickel in silicates
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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Ni in Silicates by Domain Type
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Low recovery performance in some Pentlandite samples linked
to presence of Fe-Serp, which tends to contains more nickel in
Serpentine than Mg-Serpentine (lower degree of
serpentinization)
Challenge 1: Nickel in silicates
Metallurgical Domain Average % Ni in Silicates
Haezlewoodite Dominant 37.3
Mixed Sulphide 34.1
Pn Dominant 31.1
Fe Serp Dominant 55.8
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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Feasibility Study Domaining
14 Challenge 1: Nickel in silicates Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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Challenge 2: Viscosity
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STUCK IN THE
MILL!
Challenge 2: Viscosity
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Rheology of Dumont Deposit
Tests were performed on 102 variability samples
All samples showed varying levels of “rheopexy” at higher percent solids
Rheopexy = Non Newtonian fluid behaviour where the slurry gets thicker the longer it experiences shear force
Grouped in 3 main groups
High but measurable rheopexic response (70%)
Extremely rheopexy (25%)
Thixotropic (5%)
Cause: Mg-silicate slimes generated during grinding (brucite and serpentine)
Potential Solutions
Reagents – expensive (operating costs)!
Dilution – expensive (capital costs)!
Desliming (physical separation)
Used in existing nickel ultramafic operations
Mt. Keith
Santa Rita
16 Challenge 2: Viscosity
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Desliming of Dumont Ore
Desliming was tested initially in 2008
Used a decanting method which did not provide enough energy to remove the slimes from the slurry
Wet desliming tested again in 2009 at CTMP in Thetford Mines
2” cyclone fed by a centrifugal pump
Tried various desliming mass removals
7%, 10%, 15%, 20%
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RNC Desliming Rig Set Up
Challenge 2: Viscosity
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Impact of Desliming on Metallurgical Performance
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Overall recovery is unchanged
Concentrate grade is
significantly higher
Improves cleaner performance
and reduces equipment size
STP = 7% Wt to
Slimes
KIN = 20% Wt to
Slimes
Challenge 2: Viscosity
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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Challenge 3: Flowsheet Development
Goals
Low cost
Operating and Capital
Operable
Understand ore variability
Simplify circuit where possible
Use existing technology that currently operates at similar scale
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Comminution Variability Testing
20 Challenge 3: Flowsheet Development
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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2010 Scoping Study Flowsheet
21 Challenge 3: Flowsheet Development
Source: 2010 Preliminary Assessement: Technical Report on the Dumont Ni Project dated September 30, 2010
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Dumont 2013 Feasibility Study Mill Flowsheet
Challenge 3: Flowsheet Development
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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Reagent Suite Development for Dumont
Reagent (g/tonne) 2009 Estimate
2010 Preliminary
Assessment
2012 Prefeasibility
2013 Feasibility
Xanthate 550 324 140 80
CMC 1400 704 25 6
Frother 110 86 26 91
Calgon 1000 250 50 254
Acid 0 20 8000 3900
Fuel Oil 0 1.58L/t 0 0
$CDN/tonne $7.71/t $4.70/t $1.98/t $1.78/t
23 Challenge 3: Flowsheet Development
2009 Estimate: based on initial testwork 2010 Preliminary Assessement: Technical Report on the Dumont Ni Project dated September 30, 2010 2012 Prefeasibility: Technical Report on the Dumont Ni Project dated June 22, 2012 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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Confirmation Testing with Locked Cycle Tests
24 Challenge 3: Flowsheet Development
Source : 2013 Feasibility: Technical Report on the Dumont Ni Project dated July 25, 2013.
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3D Plant Illustration - 52,500 tpd
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Conclusions
Dumont flowsheet: solutions to metallurgical challenges
Ni in Silicates
Slurry Viscosity
Focussing on the correct work during the study and flowsheet development stage reduces the risk
Understanding the deposit variability
Both in mineralogy and metallurgical response
Developing a flowsheet that is robust and able to process a range of ore characteristics in a low cost structure
Desliming
Simple reagent suite
Variability tests for key characteristics (recovery, comminution, viscosity)
Existing technology
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Acknowledgements
Royal Nickel Technical Team
Michelle Sciortino
John Korczak
Alger St. Jean
Centre de Technologie Minéral et de Plasturgie
Jovette Marois – Cégep de Thetford
SGS Minerals Lakefield
Khalil Nasrallah
Ausenco Solutions
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