Horizonte Minerals Plc, (AIM:
HZM, TSX: HZM) (‘Horizonte’ or ‘the Company’) the nickel cobalt
development Company focused in Brazil, is pleased to announce the
successful completion of the previously announced test work on
samples of limonite ore from the Company’s 100% owned Vermelho
nickel-cobalt project (‘Vermelho’) located in the southern part of
the Carajás mining district in Pará state, northern
Brazil.
Highlights:
- High purity product containing 21.8% cobalt, exceeding the
reference grade used for sulphate pricing;
- Nickel sulphate produced as a solution ready for purification
to final battery grade product.
- The results confirm the suitability of the Pressure Acid Leach
(‘PAL’) Process and subsequent purification stages for processing
Vermelho limonite ore to produce high purity cobalt and nickel
sulphate suitable to supply the EV battery markets;
- Positive results from the test work to be integrated into the
Pre-feasibility Study underway on the Vermelho Project;
and
- The results follow test work earlier in the year which also
showed that Vermelho saprolite ore is suitable for conventional
processing at the Rotary Kiln Electric Furnace ("RKEF") to be built
at the Company’s Araguaia FeNi project.
Horizonte CEO Jeremy Martin
said, “Producing high purity nickel and cobalt sulphate
from the Vermelho project of suitable quality and grade for use in
EV battery production is a major milestone in the development of
the project. The Vermelho project is a value driver for the
Company, it is a high-grade scalable resource, with good
infrastructure and has the potential to be fast tracked to
development.
The successful completion of this sulphate test
work confirms that the selected process flow sheet is suitable to
treat the Vermelho ore and when combined with the earlier
successful RKEF test work demonstrates that alternate process
routes exist for the project. The data from the test programmes
will be incorporated into the Vermelho Pre-feasibility Study, for
release in early H2, with the objective of demonstrating a robust
set of economics for the project.
The EV market continues to grow with increased
activity shown from miners and battery manufactures in securing
high quality resource projects. We see Vermelho as an
attractive strategic asset with the ability to produce nickel
sulphate and a non-conflict, ethical source of cobalt.
Elsewhere we continue to advance the project
financing (PF) on the Araguaia Ferronickel Project, with positive
interest shown from seven international banks regarding a PF
syndicate. Discussions are also underway with a number of groups on
product marketing and offtake. The overall demand picture for
nickel is robust, running at around 4% to 5% per year with
stainless steel currently accounting for two thirds of demand.
Crucially nickel inventories continue to be drawn down with the LME
levels at around 170,000 tonnes, its lowest level in 5 years with
this downward trajectory due to run through the end of the year.
The medium term consensus nickel price is around US$16,200/tonne
which, based on the Feasibility Economics on Araguaia, deliver over
US$2 billion of net cash flow over the life of mine at a C1 cash
cost of around U$6,800/t nickel placing the project in the lower
quartile of global laterite nickel operations and one of a very
limited number of scalable, high grade, fully permitted,
construction ready projects globally.
This robust demand picture for nickel positions
Horizonte well, owning 100% of two Tier 1 nickel projects, within
trucking distance of each other with the potential to produce
40,000 to 50,000 tonnes per year of nickel to service both the
traditional stainless and EV battery market as well a cobalt
revenue stream from outside of the Democratic Republic of Congo
(DRC ) and service both the traditional stainless and EV battery
market”.
Summary
The Company completed bench scale
hydrometallurgical test work at the test facilities of SGS in
Lakefield, Ontario, Canada during Q1-Q2 2019 on representative
samples of Vermelho limonite ore, averaging 1.72% Ni, 0.076% Co and
27.7% Fe. Approximately 157 kg (wet) of Vermelho limonitic ore was
received at SGS. After homogenisation, a sub-sample was taken for
full chemical analysis. The bulk sample was then scrubbed in
batches of about 25 kg using fresh water. The scrubbed ore was then
screened, with the oversize ground and recycled so that all screen
under-flow was used for the hydrometallurgical test work. It is
noted that a beneficiation step, as would be included in a
commercial plant, was not carried out in the laboratory tests.
The individual hydrometallurgical tests carried
out are briefly summarised under the following four major test
stages;
- HPAL Leaching and neutralisation of solution
- Production of Mixed Hydroxide Precipitate (MHP) and
re-leaching
- Separation of Co and Ni and purification of the Co
solution
- Cobalt sulphate crystallisation.
Detailed Information
1. PAL
Leaching and neutralisation of solution
Initially, two leach tests were carried out in a
2-litre autoclave with 400 gm of ore in order to determine
conditions for the subsequent full-scale leaching using the
20-litre test autoclave (to be carried out in ~20 individual leach
batches with about 5 kg of ore at a time).
The leach conditions used in previous work by
Vale were also taken into account. Typical leach conditions used
are presented in Table 1.
Table 1. Typical leach conditions used for the
tests
Item |
Value |
Solids, % |
35 |
Acid used, kg/t dry ore |
350-400 |
Pressure, psi |
585 |
Temperature, 0C |
250 |
Ni extraction, % |
98 |
Co extraction, % |
96 |
A total of 20 individual leach batches were
carried out to process all the ore. A typical analysis of the final
pulp filtrate is presented in Table 2.
Table 2. Typical chemical analysis of final pulp
filtrate
Element |
Analysis, mg/L |
Ni |
7,880 |
Co |
345 |
Fe |
7,660 |
Mg |
10,600 |
Al |
2,370 |
Cu |
49.2 |
Zn |
152 |
Mn |
1,490 |
Cr |
230 |
Nickel and cobalt extractions were very
high.
Two limestone scoping tests (for the primary and
secondary neutralisation) were successfully carried out to develop
the conditions for solution neutralisation. The final pH was set at
between 5 and 5.1. The primary and secondary neutralisation steps
on the bulk solution were subsequently carried out. It is noted
that in the present batch laboratory testing, a number of
sub-products were generated which were not recycled as would occur
in a continuous commercial operation; metal recovery, which is
impacted by this situation, was not to be evaluated in the present
work.
2. Production of Mixed
Hydroxide Precipitate (MHP) and re-leaching
As planned, Ca(OH)₂ was used to generate the MHP
product containing mostly Ni and Co hydroxides. The analysis of the
MHP prior to re-leaching is presented in Table 3.
Table 3. Typical chemical analysis of the
produced MHP
Element |
Analysis, % |
Ni |
18.3 |
Co |
0.97 |
Mn |
1.92 |
Mg |
0.67 |
Ca |
13.1 |
Cu |
<0.01 |
Zn |
0.12 |
3. Separation of Co and Ni
and purification of the Co solution
Solvent Extraction
Test conditions were established on small-scale
batch laboratory scoping tests. In addition, Cytec Canada Inc.
provided recommendations for test conditions. (The modelling
by Cytec recommended to use a 10% Cyanea 272 reagent in Exxsol D80
with a phase ratio of 1:1; the scrub liquor was also defined). The
solvent extraction on the bulk solution was then carried out on a
continuous basis in laboratory apparatus which was assembled for
the purpose.
Ion Exchange
Ion exchange was carried out as a two-stage ion
exchange contacting sequence. A sulphide precipitation step was
then carried out after the ion exchange step following initial
tests using a synthetic solution to determine the best conditions.
(Thermochemical computations showed that under the proposed
conditions, cobalt sulphide would precipitate ahead of that for
zinc, copper and manganese, thus affording a means of elemental
separation and purification). A further manganese removal
stage was also carried out.
4. Cobalt sulphate
crystallisation.
The near-pure cobalt sulphate solution was
crystallised batch-wise under controlled conditions and a single
harvest of cobalt sulphate crystals was gathered. This material at
over 99.91 % pure is considered ready for a final purification
stage for specific battery market applications.
Figure 1. Sample of cobalt sulphate
heptahydrate
https://www.globenewswire.com/NewsRoom/AttachmentNg/f365046f-d473-49ba-8389-557f383bcde3
For further information, visit
www.horizonteminerals.com or contact:
Horizonte Minerals plcJeremy Martin
(CEO) |
+44 (0) 203 356 2901 |
|
|
Numis Securities Ltd (NOMAD & Joint
Broker)John Prior |
+44 (0) 207 260 1000 |
Paul Gillam |
|
|
|
Shard Capital (Joint Broker)Damon Heath |
+44 (0) 20 186 9952 |
Erik Woolgar |
|
|
|
Tavistock (Financial PR)Gareth Tredway |
+44 (0) 207 920 3150 |
Annabel de Morgan |
|
About Horizonte Minerals:
Horizonte Minerals plc is an AIM and TSX-listed nickel
development company focused in Brazil. The Company is developing
the Araguaia project, as the next major ferronickel mine in Brazil,
and the Vermelho nickel-cobalt project, with the aim of being able
to supply nickel and cobalt to the EV battery market. Both projects
are 100% owned.
CAUTIONARY STATEMENT REGARDING FORWARD LOOKING
INFORMATION
Except for statements of historical fact
relating to the Company, certain information contained in this
press release constitutes "forward-looking information" under
Canadian securities legislation. Forward-looking information
includes, but is not limited to, the ability of the Company to
complete the Acquisition as described herein, statements with
respect to the potential of the Company's current or future
property mineral projects; the success of exploration and mining
activities; cost and timing of future exploration, production and
development; the estimation of mineral resources and reserves and
the ability of the Company to achieve its goals in respect of
growing its mineral resources; the ability of the Company to
complete the Placing as described herein, and the realization of
mineral resource and reserve estimates. Generally, forward-looking
information can be identified by the use of forward-looking
terminology such as "plans", "expects" or "does not expect", "is
expected", "budget", "scheduled", "estimates", "forecasts",
"intends", "anticipates" or "does not anticipate", or "believes",
or variations of such words and phrases or statements that certain
actions, events or results "may", "could", "would", "might" or
"will be taken", "occur" or "be achieved". Forward-looking
information is based on the reasonable assumptions, estimates,
analysis and opinions of management made in light of its experience
and its perception of trends, current conditions and expected
developments, as well as other factors that management believes to
be relevant and reasonable in the circumstances at the date that
such statements are made, and are inherently subject to known and
unknown risks, uncertainties and other factors that may cause the
actual results, level of activity, performance or achievements of
the Company to be materially different from those expressed or
implied by such forward-looking information, including but not
limited to risks related to: the inability of the Company to
complete the Acquisition as described herein, exploration and
mining risks, competition from competitors with greater capital;
the Company's lack of experience with respect to development-stage
mining operations; fluctuations in metal prices; uninsured risks;
environmental and other regulatory requirements; exploration,
mining and other licences; the Company's future payment
obligations; potential disputes with respect to the Company's title
to, and the area of, its mining concessions; the Company's
dependence on its ability to obtain sufficient financing in the
future; the Company's dependence on its relationships with third
parties; the Company's joint ventures; the potential of currency
fluctuations and political or economic instability in countries in
which the Company operates; currency exchange fluctuations; the
Company's ability to manage its growth effectively; the trading
market for the ordinary shares of the Company; uncertainty with
respect to the Company's plans to continue to develop its
operations and new projects; the Company's dependence on key
personnel; possible conflicts of interest of directors and officers
of the Company, the inability of the Company to complete the
Placing on the terms as described herein, and various risks
associated with the legal and regulatory framework within which the
Company operates. Although management of the Company has attempted
to identify important factors that could cause actual results to
differ materially from those contained in forward-looking
information, there may be other factors that cause results not to
be as anticipated, estimated or intended. There can be no assurance
that such statements will prove to be accurate, as actual results
and future events could differ materially f
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