VANCOUVER, British Columbia,
April 29, 2019 /CNW/ --
Highlights
- US$217 million (Cdn$290 million) after-tax Net Present Value at
8% discount rate and Internal Rate of Return of 28.0%;
- PEA based on a production rate of 5,000 tonnes of lithium
carbonate per year;
- Processing based on simple and proven solar evaporation
technology;
- Expected mine life of 30 years with a 3 year ramp up period
starting 2021;
- Fully loaded operating cost of US$3,122 per tonne of lithium carbonate;
- Total capital expenditure of US$93
million.
NRG METALS INC. ("NRG" or the "Company") (TSX-V: NGZ) (OTCQB:
NRGMD) is pleased to announce positive results from an
independent Preliminary Economic Assessment (PEA) for its Hombre
Muerto North Lithium Project near Salta, Argentina. The PEA was prepared by Knight
Piesold Consulting ("KP") and JDS Energy and Mining ("JDS"), both
of Vancouver, in accordance with
the standards set out in National Instrument 43-101 Standards of
disclosure for Mineral Projects (NI 43-101), and, CIM's Best
Practice Guidelines for Mineral Processing (BPGMP). The PEA is
preliminary in nature, and there is no certainty that the PEA will
be realized.
Company President and C.E.O Adrian F.C.
Hobkirk is quoted: "We are very pleased that NRG has
advanced the HMN Project from discovery to PEA in just under twelve
months. The PEA results highlight attractive economics associated
with the project, including a smaller environmental footprint and
manageable CAPEX. We look forward to taking the HMN Lithium Project
to the next stage of development as quickly as possible ".
Preliminary Economic Assessment Highlights
After-tax Net Present
Value (" NPV ") 8% discount rate
|
$ 217
million
|
After-tax Internal
Rate of Return ("IRR")
|
28.0%
|
CAPEX Capital
Expenditures
|
$ 93.3
million
|
OPEX Cash Operating
Costs (per metric tonne of lithium carbonate)
|
$ 3,112
|
Average Annual
Production (lithium carbonate )
|
5,000
|
Mine Life
|
30 years
|
Payback Period (from
commencement of production )
|
2 years 5
months
|
The Preliminary Economic Assessment is preliminary in nature,
there is no certainty that the Preliminary Economic Assessment will
be realized. The economic analysis is based upon mineral resources
that are measured and indicated, but are not mineral reserves, and
have not demonstrated economic viability.
Resource Estimate
The resource estimate was prepared in accordance with C.I.M.
requirements/definitions and uses best practice methods specific to
brine resources, including a reliance on core drilling and sampling
methods that yield depth-specific chemistry and effective
(drainable) porosity measurements. The resource estimation was
completed by independent qualified person Mr. Michael Rosko, M.Sc., C.P.G. of the
international hydrogeology firm E.L. Montgomery & Associates
(M&A), which was announced in a news release dated October 2, 2018, and is summarized as
follows:
Table 1. Hombre Muerto North Lithium Brine Resource
Statement
Tonnages are rounded off to the nearest 1,000. Cutoff grade:
500 mg/L lithium, but no laboratory results were less than the
cutoff grade. The conversion used to calculate the equivalents from
their metal ions is based on the molar weight for the elements
added to generate the equivalent. The equations are Li x 5.3228 =
lithium carbonate equivalent and K x 1.907 = potassium chloride
equivalent. The reader is cautioned that mineral resources are not
mineral reserves and do not have demonstrated economic
viability.
The resource is defined over a 3.9 square kilometer footprint
using results from core drilling and depth-specific packer
sampling. In addition, the brine was also sampled during short term
pumping tests. The new Measured and Indicated Resource was derived
from two polygons surrounding core holes drilled to depths of 401
and 281 meters (m). Large diameter rotary holes were drilled
adjacent to both core holes, each to a depth of about 400 m. The spacing between the two pairs of
core/rotary holes is approximately 2.1 kilometers.
Capital Costs
Description
|
$ US
Million
|
Evaporation
Ponds
|
22.8
|
Plant Facilities and
Equipment
|
31.5
|
Infrastructure and
Other
|
14.5
|
Direct Costs
Subtotal
|
68.2
|
Indirect
Costs
Total Direct and
Indirect Costs
|
11.4
79.6
|
Contingency @
17%
|
13.3
|
Total Initial
Capital Costs
|
93.4
|
Capital costs ( CAPEX ) have been updated with quotations from
current suppliers working in project construction and development
in the Puna region of Argentina. CAPEX estimates include an
Indirect Cost of 16.6% of Direct Costs, and a contingency of 17% of
Total Costs.
Operating Costs
Description
|
US$M/Year
|
Pond
Chemicals
|
8.74
|
Salt Removal and
Transport
|
0.78
|
Energy
|
1.08
|
Transportation
|
0.31
|
Maintenance
|
1.20
|
Equipment
Operation
|
0.23
|
Manpower
|
2.16
|
Catering and Camp
Costs
|
0.36
|
Total Direct
Costs
|
14.86
|
|
|
Indirect
Costs
|
|
General and
Administrative Local
|
0.70
|
|
|
Total Production
Costs
|
15.56
|
|
|
Project Location and Environmental Permitting
The Project is located at the northern portion of the Salar del
Hombre Muerto, at the boundary zone of the Catamarca and Salta
provinces, 170 km southeast of the city of Salta. The project
area comprises a collection of properties or concessions acquired
under purchase options from the existing owner. The
properties are held as "minas" (full mining licenses not subject to
further area reduction requirements) by Mr. Jorge Moreno, a private borate producer focused
on the exploration, exploitation and marketing of ulexite. The
Project comprises six properties distributed over the Salar for a
total of 3,237 hectares. All properties are subject to a mining
license for borates. The area of the Property is not subject to any
known environmental liabilities.
Lithium Pricing
Lithium prices were based on an average of three years historic
pricing and two years forward projections for battery grade
lithium. The three-year historic price (to April 2019) is $11,770 /t. Contemporary publicly available
reports have published a range of forward pricing that varies
between $10,700 to $14,750 /t for the next two years. The median
price of $13,400 /t was selected as
the forward projected price for each of the next two years. This
resulted in a project price assumption of $12,420 /t, which was used as the basis of the
study. A range of +/- 20% was evaluated to test the project's
sensitivity to price assumptions.
Recovery and Processing
The PEA models the extraction of the brine containing the
lithium resource by means of multiple extraction wells.
The brine will be pumped to a series of pre-concentration and
concentration evaporation ponds. Evaporation will increase the
lithium content and precipitate or "salt out" species such as Na,
K, and Cl. Lime will be added to the pre-concentrated brine to
remove bulk impurities such as sulphate as gypsum, which will be
physically separated. The final concentrated solution will be
stored in lithium surge evaporation ponds then pumped to a
hydrometallurgical processing plant to purify the concentrated
brine and recover the final product.
The production of lithium carbonate involves the following
steps:
- Boron removal using solvent extraction;
- Polishing of the boron-free raffinate in order to remove
impurities such as residual calcium and magnesium, among others,
using sodium carbonate (soda ash) solution,
Na2CO3;
- Lithium carbonate (Li2CO3) precipitation
('carbonation') using sodium carbonate solution
- Lithium carbonate purification by re-dissolution with carbon
dioxide and re-precipitation by desorption;
- Lithium carbonate drying, conditioning and packaging.
It was deemed that the quality of the hydrometallurgical
plant-concentrated feed-brine was superior in terms of key impurity
to lithium ratios. For this reason, stages such as bulk sulphate
polishing (using calcium or barium chloride) were excluded from the
process. The need of scavenging precipitation for magnesium using
caustic soda was also deemed redundant at this point in time.
Instead, a purification circuit was included to ensure adequate
purity of the final product, targeted as battery-grade lithium
carbonate (99.5% Li2CO3).
The entire lithium recovery process block-diagram from extraction
to packaging is illustrated below:
Qualified Person Statements
Richard Goodwin, P.Eng., Project
Manager for JDS Energy and Mining, Inc., is independent of NRG
Metals Inc.. and a 'Qualified Person' as defined under Canadian
National Instrument 43-101. Mr. Goodwin is a mining engineer and
Study manager with over 30 years of experience managing mining
operation and projects in various commodities such as base metals,
precious metals, PGMs, and diamonds in various domestic and
international locations. Mr. Goodwin is responsible for the PEA
results, participated directly in the production of this press
release, and directly related information in this press release,
and approves of the technical and scientific disclosure contained
herein.
Alex Mezei, P.Eng, is a
'Qualified Person' as defined under Canadian National Instrument
43-101, is responsible for the processing and recovery assumptions
used in the preparation of the PEA, which are disclosed in this
news release. Mr. Mezei is a Consulting Metallurgist with extensive
experience in base, precious, rare and light metals, including
lithium, cobalt, graphite, etc. Mr. Mezei is independent of NRG
Metals Inc.
The P.E.A. is the first step in moving the HMN Project towards
potential development. The process developed for the site is
based on conventional, proven technology for brine operations. The
project is located with easy access to energy, and on a salar of
development activity. Galaxy Resources Ltd. recently sold the land
surrounding the HMN Lithium Project to Korean conglomerate POSCO
for $ US 280 million and are continuing to develop their remaining
portion of the salar, referred to as the Sal da Vida Project. The
project is located in a jurisdiction that is mining friendly
(Salta Province), and the Government
of Argentina recently announced
reducing the corporate tax rate for mining companies to 25% in
2020.
The final report is expected to be completed within the next 45
days and filed on SEDAR. Pending completion of the report, the
Company intends to rapidly advance the HMN Lithium Project to a
full feasibility study which will include upgrading the current
resource to a reserve status. Pilot test work to develop the basic
engineering will be performed with the intent of producing a
Battery Grade Lithium Carbonate (99.5% Li2CO3
purity).
On behalf of the board of directors of NRG Metals Inc.
Adrian F. C. Hobkirk
President and Chief Executive Officer
The TSX Venture Exchange has not reviewed the content of this
news release and therefore does not accept responsibility or
liability for the adequacy or accuracy of the contents of this news
release.
This news release contains certain "forward- looking statements"
within the meaning of Section 21E of the United States Securities
and Exchange Act of 1934, as amended. Except for statements of
historical fact relating to the Company, certain information
contained herein constitutes forward- looking statements.
Forward-looking statements are based upon opinions and estimates of
management at the date the statements are made and are subject to a
variety of risks and uncertainties and other factors which could
cause actual results to differ materially from those projected in
the forward looking statements. The reader is cautioned not to
place undue reliance on forward- looking statements. We seek safe
harbor.
Investors / Shareholders Call 855-415-8100 or direct to
Adrian Hobkirk 714-316-3272
ahobkirk@nrgmetalsinc.com
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SOURCE NRG Metals Inc.