22 July
2024
CleanTech Lithium PLC ("CleanTech
Lithium", "CTL" or the "Company")
DLE Pilot Plant First Stage Production
Completed, Downstream Process Optimised
with Sample of Battery-Grade Lithium
Produced
CleanTech Lithium PLC (AIM:CTL, Frankfurt:T2N,
OTCQX:CTLHF), an exploration and development
company advancing sustainable
lithium projects in Chile, announces completion of the first stage
of production from the Company´s DLE pilot plant operations and
results from successful downstream process test work to produce
battery-grade lithium carbonate by process partners in North
America.
Highlights:
· An
initial volume of 88m3 of concentrated eluate, which is
the lithium carbonate equivalent (LCE) of approx. one tonne, has
been produced from the Company´s DLE pilot plant in Copiapó, Chile
over an operating period of 384 hours with 14 cycles
completed
·
This completes the first stage of production from the DLE
pilot plant
·
Results show the DLE adsorbent achieved a lithium
recovery rate of approximately 95% from the brine, with total
recovery (adsorption plus desorption) achieving approximately
88%
·
Impurity rejection rates were very high producing a low
impurity eluate conducive to the downstream conversion
process.
· The
concentrated eluate is being shipped in four batches to the
facilities of Conductive Energy in Chicago, USA, for conversion
into battery grade lithium carbonate
Shipment
|
Eluate
Volume
|
Eluate Li
Grade
|
LCE
(kg)
|
Shipment
Status
|
1
|
24m3
|
2008 mg/L
|
257
|
Arrived process facility
|
2
|
24m3
|
2360 mg/L
|
301
|
In Shipment
|
3
|
24m3
|
2325 mg/L
|
297
|
In shipment
|
4
|
17.5m3
|
2464 mg/L
|
230
|
At departure port
|
Targeted
|
90m3
|
2000 mg/L
|
1022
|
|
Total Achieved
|
88m3
|
2289 mg/L
|
1085
|
|
Table 1:
Status of concentrated eluate from pilot plant first stage
production
·
Conductive Energy completed test-work on a 200L sample of
concentrated eluate shipped in May 2024 to optimise the downstream
process before receiving the larger volume shipments
· The
conversion test-work produced multiple samples of lithium carbonate
with 99.75% lithium carbonate purity demonstrating that the process
achieves targets and is repeatable
· The
result is a first confirmation that a process has been developed
that will efficiently produce battery-grade lithium for the Laguna
Verde project from pilot scale DLE eluate
·
CleanTech Lithium continues to be a leader in exploration and
development of DLE based projects in Chile and this pilot scale
production will provide large test samples of lithium carbonate to
potential offtake partners seeking product
qualification.
·
Subject to the completion of the re-injection well in
September, the reserve report for Laguna Verde is scheduled to be
completed by Montgomery and Associates in October 2024.
Steve Kesler,
Executive Chairman and Interim CEO, of CleanTech Lithium PLC,
said:
"We are very
pleased by these results as it shows we can produce battery-grade
lithium with low impurities from our Laguna Verde brine project.
Working with our partners on the downstream process, Forward Water
and Conductive Energy, we can now demonstrate the entire DLE
process from brine to final lithium product.
"The
optimised downstream process will now be applied to the initial
volume of 88m3 of concentrated eluate, or approximately
1 tonne of LCE, produced from the first stage of production from
our DLE pilot plant. This will produce significant test sample
volumes of battery-grade lithium carbonate for commencement of
testing with potential strategic partners. This is important whilst
the Chilean government is reviewing the feasibility of lithium
projects to identify the most advanced companies in Chile and if
they are to reach their target of having three to four new lithium
projects in development by 2026."
Further
Information
Pilot Plant in Copiapó First Stage Production
Completed
The Company´s DLE pilot plant is
in Copiapó, Chile,
approximately 275km from Laguna Verde. The plant finished
commissioning in late March 2024 and up until mid-June a total
volume of 1196m3 of brine from the Laguna Verde project
was processed in the plant with a total of 14 cycles completed.
Each cycle represents a volume of brine being fed first through
filtration to remove suspended solids, then into DLE columns which
are filled with adsorbent designed to be selective for lithium
molecules. Lithium, as lithium chloride, is adsorbed from the
brine, before desorption with water to create a purified lithium
chloride eluate. A reverse osmosis (RO) unit at the DLE pilot
plant then concentrates the eluate by extracting
approximately 75% of the water to form a concentrated
eluate.
Averaged across the 14 cycles, the recovery
rate achieved by adsorption of lithium by the adsorbent was 95% and
the recovery rate of desorption from the adsorbent was 93%. The
total recovery rate averaged 88% and was highly consistent as shown
in Figure 1. The temperature of the brine and desorption water,
using the average ambient temperature in Copiapó during the March
to June period of operation, was in the range of 20oC to
25oC, which did not significantly affect the recovery
achieved.
Figure 1:
Pilot Plant Total Recovery Rate
The eluate production rate was relatively
stable after the initial ramp up period achieving an average of 2.8
kg LCE per hour. The design of the plant is 1 tonne per month of
LCE based on designed monthly operating schedule of 360 hours. Due
to budget and volume considerations, the plant was run for 384
hours for the first stage of planned operation producing a total of
1.085 tonnes of LCE as eluate. Based on the hourly production rate
this met and exceeded the design capacity of the plant.
Figure 2:
Pilot Plant Production Rate (Kg LCE/hr in Eluate)
Selectivity of the adsorbent is another key
performance parameter for a DLE operation. DLE
primarily acts as a purification stage, recovering lithium chloride
from the brine whilst rejecting other impurities. For all the major
ions in the brine, apart from boron, the rejection rate was very
high as shown in Fig. 3 below. More cycles will further validate
this performance. The quality of the eluate was consistent over the
first stage of production with the low level of impurities
facilitating downstream conversion.
Figure 3: DLE
Performance - Rejection of Major Impurities
After completion of the DLE stage,
the eluate is concentrated using a reverse osmosis (RO) unit at the
pilot plant. On completion of both stages the lithium grade in the
purified lithium chloride eluate is over ten times higher than the
feed brine. The concentrated eluate was then loaded into a
flexitank in a standard shipping container and transported to the
port of Caldera for shipment to North America.
Downstream Processing into Battery Grade Lithium
Carbonate: Test-work Completed
For the conversion of the
concentrated lithium chloride eluate into battery grade lithium
carbonate, CleanTech Lithium has engaged a leading lithium
processing company, Conductive Energy, based in Alberta, Canada,
which has facilities in Chicago, USA, with key downstream
processing units shown in Figure 4 below. The status of the concentrated
eluate shipment is shown in Table 1 with processing to commence in
August 2024.
Figure 4: Conductive Energy Carbonation Reactor Tank and
Equipment for Washing, Filtering & Drying
In May 2024 CTL air-freighted a 200L
sample of concentrated eluate from the pilot plant to Conductive
Energy to undertake test-work to optimise the conversion process.
The process steps are shown in Figure 5, involving a further stage
of RO, before using Forward Osmosis (FO) to achieve a very high
level of concentration. Ion exchange (IX) is used to remove
calcium, magnesium, and boron. The final steps are carbonation and
then washing, filtration and drying to produce a battery grade
product. Conductive Energy´s approach is to simplify the process
that achieves maximum yield by minimizing process steps and, where
losses occur, produce fluids that are easily recycled to further
maximize yield.
Figure 5: Conductive Energy Conversion
Process
Reverse Osmosis and Forward Osmosis
The increase in eluate and lithium
concentration in the R/O and F/O stages are shown in Table 2 below.
R/O is effective for concentration until Total Dissolved Solids
(TDS) reach the level of approximately 60,000 - 70,000 TDS, after
which it is increasingly energy intensive and costly. F/O is highly
effective in further concentration to the required lithium grade
for carbonation, in this case 18,000mg Li/L (or 1.8% Lithium). The
F/O unit is provided by Forward Water Technology, another Canadian
company based in Ontario. F/O achieves a high concentration factor
with much lower energy use than the alternative of using a
mechanical evaporator, while being highly suitable for utilising
solar thermal as the energy source to power the F/O process.
Parameter
|
Unit
|
Concentrated Eluate
|
R/O
Concentrate
|
F/O
Concentrate
|
Lithium (Li)
|
mg/L
|
2,194
|
5,700
|
18,000
|
Chloride (Cl)
|
mg/L
|
11,039
|
37,000
|
110,000
|
Boron (B)
|
mg/L
|
411
|
850
|
1,700
|
Calcium (Ca)
|
mg/L
|
7
|
29
|
85
|
Magnesium (Mg)
|
mg/L
|
14
|
50
|
150
|
Sodium (Na)
|
mg/L
|
134
|
400
|
1,400
|
Sulphate (SO4)
|
mg/L
|
103
|
120
|
330
|
Total Dissolve Solids
(TDS)
|
mg/L
|
19,260
|
62,000
|
190,000
|
Volume
|
L
|
215.5
|
66.3
|
13.9
|
Reduction in Volume
|
%
|
|
69.3%
|
93.5%
|
Laboratory
|
|
ALS Chile
|
Lambton.Scientific
|
Lambton.Scientific
|
Table 2: Results from concentration of Laguna Verde eluate
through R/O followed by F/O
Ion
Exchange to Remove Impurities
Ion exchange (IX) was used for
removal of calcium and magnesium, which achieved 85% and 87%
reductions respectively. While feed concentrations
were low, 100% of barium and manganese were also removed in the
same process. Additional optimization is possible with potential
for further calcium removal. Lithium loss was low at
3%.
Conductive then applied its optimised IX for
removal of boron. This was highly effective achieving
>99.5% removal of boron. However, there was a 22% loss of
lithium to the regeneration fluid. This would be recaptured by
recycling the regeneration fluid to the F/O feed which was not
implemented for this small-scale test-work. The lithium loss from
the boron IX is expected to be reduced (recovered) to a steady
state loss rate of about 3%.
Carbonation and Battery Grade Lithium Sample
The carbonation test-work achieved an
exceptional yield of 96% of the theoretical maximum. The final
product, after the wash procedure, was 99.75% lithium carbonate
purity as shown in Table 3. Further optimisation of the
washing stage is planned in order to reduce impurities to the
greatest extent possible and therefore maximise the value of the
battery grade product.
Table 3:
Process test-work lithium carbonate sample
purity Fig.
6: Test-work sample
Additional
Operations
Laguna Verde Reserve Report
Update
The next stage of resource evaluation at the
Laguna Verde project is to produce an updated JORC compliant
resource and a reserve report based on converting a portion of
resources into reserves. The management of the resource
evaluation programme and reserve report is led by Montgomery and
Associates, a leading hydrogeology consultant with extensive
experience in resource evaluation of lithium brine projects
in Chile and Argentina. Reserve estimation will feed
directly into the Pre-Feasibility Study which is targeted for later
this year.
The reserve calculation requires the completion
of pumping tests and a re-injection well at the project which is
scheduled for September 2024, when drilling equipment can be
re-mobilised after the current winter break in operations. Subject
to the completion of the re-injection well in September, the
reserve report is scheduled to be completed by Montgomery and
Associates in October 2024.
Competent
Persons
The following professional acts as qualified
person, as defined in the AIM Note for Mining, Oil and Gas
Companies (June 2009) and JORC Code (2012):
Marcelo Bravo: Chemical Engineer (Universidad
Católica del Norte), has a Master's Degree in Engineering Sciences
major in Mineral Processing, Universidad de Antofagasta. He
currently works as a Senior Process Consulting Engineer at the
Ad-Infinitum company. Mr Bravo has relevant experience in
researching and developing potassium, lithium carbonate, and solar
evapo-concentration design processes in Chile, Argentina, and
Bolivia. Mr Bravo, who has reviewed and approved the information
contained in the chapters relevant to his expertise contained in
this announcement, is registered with No. 412 in the public
registry of Competent Persons in Mining Resources and Reserves per
the Law of Persons Competent and its Regulations in force in Chile.
Mr Bravo has sufficient experience relevant to the metallurgical
tests and the type of subsequent processing of the extracted brines
under consideration and to the activity being carried out to
qualify as a competent person, as defined in the JORC Code. Mr
Bravo consents to the inclusion in the press release of the matters
based on his information in the form and context in which it
appears.
The
information communicated within this announcement is deemed to
constitute inside information as stipulated under the Market Abuse
Regulations (EU) No 596/2014 which is part of UK law by virtue of
the European Union (Withdrawal) Act 2018. Upon publication of this
announcement, this inside information is now considered to be in
the public domain. The person who arranged for the release of this
announcement on behalf of the Company was Gordon Stein, Director
and CFO.
For
further information contact:
|
|
CleanTech Lithium PLC
|
|
Steve Kesler/Gordon Stein/Nick
Baxter
|
Jersey office: +44 (0) 1534 668
321
Chile office:
+562-32239222
|
|
Or via Celicourt
|
Celicourt Communications
Felicity Winkles/Philip Dennis/Ali
AlQahtani
|
+44 (0) 20 7770 6424
cleantech@celicourt.uk
|
Beaumont Cornish Limited (Nominated Adviser)
Roland Cornish/Asia
Szusciak
|
+44 (0) 20 7628 3396
|
Fox-Davies Capital Limited (Joint Broker)
Daniel Fox-Davies
|
+44 (0) 20 3884 8450
daniel@fox-davies.com
|
Canaccord Genuity (Joint Broker)
James Asensio
|
+44 (0) 20 7523 4680
|
Beaumont Cornish Limited ("Beaumont Cornish") is the Company's
Nominated Adviser and is authorised and regulated by the FCA.
Beaumont Cornish's responsibilities as the Company's Nominated
Adviser, including a responsibility to advise and guide the Company
on its responsibilities under the AIM Rules for Companies and AIM
Rules for Nominated Advisers, are owed solely to the London Stock
Exchange. Beaumont Cornish is not acting for and will not be
responsible to any other persons for providing protections afforded
to customers of Beaumont Cornish nor for advising them in relation
to the proposed arrangements described in this announcement or any
matter referred to in it.
Notes
CleanTech Lithium (AIM:CTL,
Frankfurt:T2N, OTCQX:CTLHF) is an exploration and development
company advancing sustainable lithium projects
in Chile for the clean energy transition. Committed to
net-zero, CleanTech Lithium's mission is to produce material
quantities of sustainable battery grade lithium products using
Direct Lithium Extraction technology powered by renewable energy.
The Company plans to be a leading supplier of 'green' lithium to
the EV and battery manufacturing market.
CleanTech Lithium has two key
lithium projects in Chile, Laguna Verde and Viento Andino, and hold
licences in Llamara and Salar de Atacama, located in the
lithium triangle, a leading centre for battery grade lithium
production. The two major projects: Laguna Verde and Viento
Andino are situated within basins controlled by the Company,
which affords significant potential development and operational
advantages. All four projects have direct access to existing
infrastructure and renewable power.
CleanTech Lithium is committed to
using renewable power for processing and reducing the environmental
impact of its lithium production by utilising Direct Lithium
Extraction with reinjection of spent brine. Direct Lithium
Extraction is a transformative technology which removes lithium
from brine, with higher recoveries than conventional extraction
processes. The method offers short development lead times with no
extensive site construction or evaporation pond development so
there is minimal water depletion from the
aquifer. www.ctlithium.com
**ENDS**