19 June 2024
Rainbow Rare Earths
Limited
("Rainbow" or "the Company")
LSE: RBW
Pilot Plant
Update
Latest results support
expectation that Phalaborwa will be one of the lowest cost magnet
rare earth projects in development today
· Primary pilot plant campaign in South
Africa ran for an extended period allowing for key optimisation
opportunities, with expected resultant benefits to capital and
operating costs
· Separation pilot plant campaign in USA
is ongoing - separation of Nd/Pr has now reached over 95% purity
via an optimised first stage chromatography step, with the process
expected to reach the targeted purity of 99.5%
· Piloting campaign to date supports our
expectation that Phalaborwa will be a low-cost producer of
separated rare earth oxides in comparison to the global peer
group
·
As part of the work to
deliver the DFS in H1 2025, Rainbow plans to release an interim
report in H2 2024 to update the economics of the Phalaborwa project
reflecting the optimisations delivered from the pilot test work
campaigns, footprinted against the Preliminary Economic Assessment
("PEA"), and to allow for commencement of project
financing
NEWS
RELEASE
Rainbow is pleased to announce an update with
regards to the pilot plant operations for the Phalaborwa rare
earths development project in South Africa.
The project's pilot plant incorporates the
primary campaign, which processes the material to produce a mixed
rare earth carbonate ("MREC"), based at the
Johannesburg facilities of the Council for Mineral Technology
("Mintek"), a global leader in mineral processing, extractive
metallurgy, and related fields. The final separation stage pilot
plant refines the material further into separated rare earth
oxides; this work is ongoing in Florida, USA.
Primary pilot
plant - Johannesburg, South Africa
Excellent results have been achieved on the
large scale, continuous pilot plant at Mintek, serving
to confirm the basic process flowsheet originally set
out in the PEA.
The primary pilot plant campaign was extended
to run for 70 days in order to take advantage of key optimisation
opportunities that became evident during the operation.
The key findings from the primary pilot plant
campaign are:
· The
overall recovery of rare earths was 66% versus 65% used in the
PEA.
· A
leach temperature of 30oC was employed compared to
40oC set out in the PEA, resulting in a 50% reduction in
the expected heating energy requirement.
· The
first-stage impurity leach readily controlled the impurities to the
desired level. Approximately 23% of the recovered rare earths
reported to the impurity leach solution.
· The
subsequent rare earths leach has been reduced from three stages in
the PEA to two stages.
· A
continuous ion exchange ("CIX") pilot plant operation was conducted
at Mintek to recover the rare earths in the impurity leach
solution. This CIX pilot plant delivered excellent recovery,
impurity rejection and rare earths upgrading with the resulting
product being suitable for feed directly to the final continuous
ion chromatography ("CIC") separation process.
·
Solid:liquid separation tests conducted on
samples from the primary pilot plant operation yielded excellent
thickening and filtration results, which allows for the removal of
six CCL (Counter Current Leach) thickeners out of 12 from the
circuit.
·
Very positive results were achieved in a materials of
construction study where a variety of potential acid-proof steels
and alloys have been tested in static conditions and in the
continuous primary pilot plant operation. These have shown that
lower cost alloys out-perform the high cost Hastelloy materials
assumed for the construction of the plant in the PEA.
Separation
pilot plant - Lakeland, USA
In parallel with the work at Mintek, test work
is ongoing at K-Technologies, Inc. ("K-Tech") premises in Florida,
USA, to deliver separated magnet rare earth oxides, with the
initial focus on the separation and purification of neodymium and
praseodymium ("Nd/Pr") via ion chromatography in three stages to an
expected 99.5% oxide purity. This represents ca. 20% of the total
processing footprint.
As previously announced on 5 February 2024, the
initial first-stage ion chromatography step achieved good
separation of Nd/Pr at ca. 68% purity, with good separation of the
samarium/europium/gadolinium ("SEG") group of rare earths at a
grade of ca. 63% and considerable upgrading of the concentration of
the dysprosium and terbium ("Dy/Tb") from a combined feed grade of
0.9% to 14.6%.
The initial 68% Nd/Pr purity stream has been
passed through a second ion chromatography stage, resulting in an
upgraded solution of over 96% Nd/Pr purity.
Optimisation of the first stage ion
chromatography step has been carried out in parallel, resulting in
an excellent Nd/Pr grade of over 95% purity.
The separation test programme in Florida is
taking longer than anticipated, primarily due to problems with the
in-house analytical equipment at K-Tech's premises. This has
resulted in the need for the material to be independently analysed
by the Florida Institute of Phosphate Research ("FIPR"), which has
required a long turnaround for each set of assays (two to three
weeks versus the anticipated one to two days if doing this work
in-house). This issue is being remediated, but there is benefit to
the extra level of verification that these independent analyses
provide to the rare earth separation work.
Dave Dodd,
Technical Director, commented: "We are very pleased with the results
of the completed primary pilot plant campaign that has produced a
high grade MREC for the separation pilot plant in the USA. The
significant results, including lower leach temperatures, the
reduced number of stages in the main rare earth leach, reduced
thickener requirements and lower cost materials of construction,
are expected to deliver capital and operating cost benefits
compared to the base case scenario for these processes set out in
the PEA.
The excellent
performance of the pilot CIX plant at Mintek, coupled with the very
good rare earth group separation and 95% Nd/Pr purity achieved by
the optimised first pass of ion chromatography work in US, auger
well for the finalisation of the CIX/CIC process and validate
Rainbow's use of CIX/CIC as our chosen rare earth recovery method.
Based on the recoveries to date, we also do not anticipate any
material changes to the capital and operating costs for the
back-end plant process."
George
Bennett, CEO, commented: "Whilst the pilot test work has taken
longer to complete than originally planned, the positives of the
additional time invested, in pursuing the optimisation
opportunities identified on the primary pilot plant, cannot be
underestimated from the point of view of confirming capital and
operating costs for the Definitive Feasibility Study ("DFS") within
the PEA guidelines.
We feel these
results go a long way to confirming that Phalaborwa will be one of
the highest margin and lowest cost rare earth producers in the
world, which gives the project excellent resilience versus pricing
volatility, in contrast to the global peer group. These results
confirm and vindicate the time invested in the process optimisation
to the benefit of the project."
Next
steps
Work is continuing in both South Africa and the
USA to finalise the pilot testing and optimisation opportunities
resulting therefrom.
South Africa
·
Initial acid baking of the rare earths precipitate, conducted
in a standard muffle furnace, required a bake time of six to seven
hours. Subsequent ongoing testing of a continuous infra-red furnace
indicates excellent results which should reduce baking time to less
than one hour.
·
Optimisation work is being undertaken in relation to the two
key reagents for the process: sulphuric acid consumption and lime
addition for neutralisation.
USA
·
Nd/Pr separation work via CIC is continuing, focused
initially on delivering the expected 99.5% purity Nd/Pr
oxide.
·
Once the Nd/Pr separation is confirmed, CIC work focused on
the Dy/Tb streams will progress as well as further work on the SEG
group separation where Rainbow saw positive results in the first
pass through the ion chromatography phase.
Following completion of the piloting testwork,
as part of the work to deliver the DFS in H1 2025, Rainbow plans to
release an interim report in H2 2024 to update the economics of the
Phalaborwa project reflecting the optimisations delivered from the
pilot test work campaigns, footprinted against the PEA. This is
expected to demonstrate the resilience of the project economics in
a variety of rare earth pricing scenarios and allow for the
commencement of the financing process for the project.
For further
information, please contact:
Rainbow Rare
Earths Ltd
|
Company
|
George Bennett
Pete Gardner
|
+27 82 652 8526
|
|
IR
|
Cathy Malins
|
+44 7876 796 629
cathym@rainbowrareearths.com
|
Berenberg
|
Broker
|
Matthew Armitt
Jennifer Lee
|
+44 (0) 20 3207 7800
|
Stifel
|
Broker
|
Ashton Clanfield
Varun Talwar
|
+44 20 7710 7600
|
Tavistock
Communications
|
PR/IR
|
Charles Vivian
Tara Vivian-Neal
|
+44 (0) 20 7920 3150
rainbowrareearths@tavistock.co.uk
|
Notes to
Editors:
About
Rainbow:
Rainbow Rare Earths aims to be a forerunner in
the establishment of an independent and ethical supply chain of the
rare earth elements that are driving the green energy transition.
It is doing this successfully via the identification and
development of secondary rare earth deposits that can be brought
into production quicker and at a lower cost than traditional hard
rock mining projects, with a focus on the permanent magnet rare
earth elements neodymium and praseodymium, dysprosium and
terbium.
The Company is focused on the development of
the Phalaborwa Rare Earths Project in South Africa and the earlier
stage Uberaba Project in Brazil. Both projects entail the recovery
of rare earths from phosphogypsum stacks that occur as the
by-product of phosphoric acid production, with the original source
rock for both deposits being a hardrock carbonatite. Rainbow
intends to use a continuous ion exchange / continuous ion
chromatography separation technique, which simplifies the process
of producing separated rare earth oxides (versus traditional
solvent extraction), leading to cost and environmental
benefits.
The Phalaborwa Preliminary Economic Assessment
has confirmed strong base line economics for the project, which has
a base case NPV10 of US$627 million, an average EBITDA operating
margin of 75% and a payback period of < two years.
More information is available at
www.rainbowrareearths.com.