Lithium X Energy
Written by
Lithium X Energy |
Argentinian brine play, fully funded to feasibility |
Mining prospects |
Metals & mining |
13 October 2016 |
Share price performance
Business description
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Lithium X Energy is a research client of Edison Investment Research Limited |
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Lithium X Energy (LIX) is currently completing fully funded exploration and development programmes at two lithium brine projects, Clayton Valley in Nevada and the flagship Sal de Los Angeles project in the world-renowned lithium triangle, specifically Salta in Argentina. With equity raisings capitalising on the recent strength of the lithium sector, it is fully funded to feasibility on Los Angeles and to fulfil its share of exploration obligations in Clayton Valley. A new NI 43-101 Sal de Los Angeles resource of 2.0Mt LCE has been announced, which provides sufficient resource confidence to complete a feasibility study on the project (now underway).
Brine projects in two proven mining locations
Both of Lithium X’s projects are in proven lithium mining jurisdictions. Sal de Los Angeles is located in the lithium triangle of Latin America, home to a number of development and production stage projects such as Fenix (NYSE:FMC), Sal de Vida (ASX:GXY), Salar de Cauchari-Olaroz (TSX-V:LAC/NYSE:SQM) and Sal de Olaroz (ASX:ORE). The Clayton Valley projects lie on the north and southern boundaries of the US’s only lithium mine, Silver Peak, owned by Albemarle.
Lithium focus increases towards larger vehicle uses
Numerous developments continue to enhance the prospects of the lithium mining sector, albeit with one caveat: the level of lithium demand required to underpin current investment is yet to occur. We view 2017 as a pivotal year for understanding how much of the current market sentiment around lithium will translate into cash flows for the mining sector, driven primarily from production numbers due from Tesla Motors in late 2017 as sales of the hugely anticipated Model 3 start. Further, the promotion of other uses for lithium, including a focus on public transport and trucks, could provide the next step change in lithium demand expectations. The latter is relevant to China, where city smog plays an important role in guiding public policy towards increasing the role of electric vehicles.
Resource indicates favourable quality and quantity
Lithium X announced, on 30 August 2016, a new resource estimate for its Sal de Los Angeles project. This new NI 43-101 compliant resource estimate supersedes the historical non-compliant 2.8Mt lithium carbonate equivalent (LCE) resource estimate previously cited by the company. The new resource estimate states c 2.0MT of recoverable LCE spread roughly equally across the indicated and inferred resource categories. Technical characteristics indicate a 12.2% yield (ie a measurement of drainable porosity across the resource), an average magnesium to lithium ratio of 3.8 and an average sulphate to lithium ratio of 14.6. All three of these measurements are well within industry norms for similar salars, indicating a low-impurity, and by extension higher-quality, sizeable brine resource. The brine also contains a meaningful amount of potassium chloride that could be sold into a local fertiliser market and provide a significant by-product credit once production starts. Studies into the cost of extraction and processing of the Diablillos brine, as well as mine and well field designs, are currently the focus of a feasibility study, currently underway (completion date to be confirmed).
Lithium X: Developing brines in lithium mining regions
Latin America, through its natural abundance and concentration of lithium in numerous salt lakes (salars), produced 48% of global lithium supply based on USGS estimates for 2015. The main contributors to Latin American production were SQM, Albemarle (previously by Rockwood), FMC Corp and new entrant Orocobre. Lithium X is well positioned with its Sal de Los Angeles project in Argentina and its Clayton Valley, Nevada, projects. Both regions play to the expanding North American electric vehicle market and to the lower-carbon future legislated in the Paris COP 21 climate agreement and recently ratified by the two largest polluters, China and the US.
Sal de Los Angeles: Well developed lithium area
Lithium X’s flagship project is called Sal de Los Angeles and covers 95% of the Diablillos salar (salt lake) in the Salta province in north-west Argentina. The company currently owns 50% of this project with an option to increase this to 80% (see pages 11 & 12). The brine is enriched not only in lithium, but also potassium, a saleable product in its own right and a likely by-product credit to any future brine operation. No historical lithium extraction from Los Diablillos has occurred, and only small-scale mining of the borate mineral ulexite has taken place via <1m deep pits. The project was most recently investigated by Rodinia Lithium, which spent US$17.2m on the project between 2010 and 2015. Works comprised 140 auger holes, 23 reverse circulation holes, seven diamond holes and 16 monitoring and pumping well tests. Gravity and seismic surveys were also conducted over the area.
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Exhibit 1: Location of Sal de Los Angeles project and regional lithium projects |
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Source: Lithium X Energy |
The Diablillos salar is located east of Ratones Hill at an altitude of 4,000m above mean sea level and is situated within an endorheic or closed basin, meaning that the only outflow from the basin occurs as evaporation, and inflows are primarily from only one source – the Diablillos River. Rainfall is minimal with anecdotal records from third parties suggesting annual rainfall of only 70-80mm pa. Los Diablillos brine fluids are stated (Rodinia Lithium 2011 PEA) as containing 16% salts (by weight) and 84% water. The basin itself covers 416km2 of which 33km2 correspond to the salar environment.
The Diablillos salar is enriched in lithium, borates and potash. In 2011, the previous owners of the project, Rodinia Lithium, commissioned a preliminary economic assessment (PEA) that contemplated an operation that produces all three. We understand that Lithium X places little value on borates due to the minimal value they currently fetch at market. The newly announced resource estimate does state a sizeable potash component that could be extracted alongside processing brine fluids for the lithium component.
A historical resource estimate was completed by Rodinia Lithium and given in an announcement dated 1 April 2011. The historical resource stated 2.8Mt LCE were contained solely within the inferred resource category. Since acquiring the deposit, Lithium X has undertaken additional drilling and technical work to upgrade a portion of the resource from inferred to indicated. With 1Mt LCE now classified as indicated, Lithium X is now able to initiate work to complete a feasibility study. Feasibility studies cannot be signed off if only inferred resources are stated; indicated and measured resource categories are the only categories with a high enough confidence level to be converted into ore reserves under NI 43-101 guidelines.
Lithium X’s updated mineral resource estimate, which follows current Canadian NI 43-101 guidelines, is provided in Exhibit 2 below. This revised estimate has incorporated new pump test data undertaken by SRK Consultants and FloSolutions and also some data from drilling on the northern half of the salar where the company states the resource is still open to further expansion.
Exhibit 2: NI 43-101 Mineral Resource estimate, prepared by FloSolutions (Chile), effective date of estimate 29 August 2016
Indicated |
Inferred |
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Lithium |
Potassium |
Boron |
Lithium |
Potassium |
Boron |
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Aquifer area (km2) |
22.2 |
32.4 |
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Aquifer volume (km3) |
3.2 |
3.8 |
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Mean specific yield (%) |
12.2 |
12.0 |
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Brine volume (km3) |
0.4 |
0.5 |
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Mean grade (g/m3) |
60.8 |
668.5 |
67.6 |
49.3 |
539.0 |
60.7 |
Equivalent concentration (mg/L) |
501 |
5,512 |
556 |
410 |
4,489 |
505 |
Resource (tonnes) |
194,860 |
2,143,491 |
216,807 |
189,130 |
2,068,161 |
232,601 |
Resource (LCE tonnes) |
1,034,634 |
1,006,172 |
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Grand total (LCE tonnes) |
2,040,805 |
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Source: Lithium X 30 August 2016 announcement. Note: Slight differences may occur due to rounding.
Ponding facility trial
Critical to the success of any lithium operation is the production of commercial-scale volumes of lithium end products prior to full-scale development. As with many technology metals, from rare earths to zirconium, consistency and quality are key and products must meet strict criteria, especially if used for the production of lithium-ion batteries that are required to last the 100,000+ mile term of a road car. The ponding facility trial will also provide Lithium X with key data, which is critical to understanding evaporation rates at the project’s altitude of c 4,000m amsl (metres above mean sea level).
On 20 April 2016 Lithium X completed its acquisition of an initial 50% interest in Potasio y Litio de Argentina (PLASA), which owns 100% of Sal de Los Angeles, from Aberdeen International. PLASA entered into a JV agreement with Salta Exploraciones (SESA) for the development of a pilot lithium carbonate plant at Sal de Los Angeles. The pilot plant requires final permit approvals to be obtained before production can start. Once pilot plant production has started it will run for 25 years at a maximum rate of 2,500tpa LCE unless decided by the governing committee to increase to 5,000tpa LCE.
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Exhibit 3: Lithium X ponding facility trial JV structure with partner, SESA |
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Source: Lithium X corporate presentation. Note: LIX owns 50% of PLASA with an option to increase to 80%. |
Clayton Valley (north and south), Nevada
Lithium X’s second project comprises two claim areas, situated directly north (Clayton Valley North) and south (Clayton Valley South) of Albemarle’s Silver Peak lithium brine operation.
The history of Silver Peak dates back to the latter half of the 19th century when a mine was built to extract gold, silver and other minerals and helped to establish a settlement of the same name in 1864. The Silver Peak mine provides an indication of the scale of a future brine well-field and associated evaporation ponds for any future operation owned by Lithium X in the area. Silver Peak pumps brines from its well-field to the evaporation ponds, which cover c 4,000ha. The brine naturally evaporates and concentrates using only sunlight. Once the brine is suitably concentrated in salts, it is pumped to a processing plant where it is treated with soda ash used to precipitate the lithium carbonate.
The following sections outline Lithium X’s ownership of each claim area and any obligations it has over their development and funding.
Clayton Valley North
Clayton Valley North is at the exploration stage, with Lithium X undertaking a Phase 1 exploration programme, comprising the drilling of one hole with a further three holes contingent on the results of the first. Lithium X will also investigate the lowest gravel aquifer, which management states shows “strong potential” in terms of brine content.
The lower gravel aquifer is expected to be intersected at a depth of approximately 350m, which we consider should take 10 days to two weeks to complete, assuming minimal stoppages and drilling on only one shift.
Lithium X has an option to acquire a 100% interest in the NSP Lithium Claim Group from Clayton Valley Lithium (CVL), a private company. In order to exercise this option Lithium X must:
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Pay US$0.25m in cash to CVL on the first, second, third and fourth anniversaries of the deal’s closing date.
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Issue 446,113 common shares to CVL on each of the first, second, third and fourth anniversaries of the deal’s closing date.
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Spend US$4.5m on exploration expenditures on the NSP Lithium Claim group over a three-year period and deliver a PFS on the NSP Lithium Claim Group by no later than the fourth anniversary of the closing date.
Other payments that are or could be due by Lithium X to CVL are:
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LIX has agreed to the issue of 1m shares to CVL on definition and completion of an inferred resource of a minimum 100,000t LCE at a minimum Li concentration of 28 parts per million.
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LIX shall pay US$2m in cash or shares or a combination thereof on completion of a positive feasibility study on the NSP Lithium Claim Group.
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CVL will be granted a 2.5% royalty on revenues on the production of lithium or any other mineral from the NSP Lithium Claim Group.
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LIX has agreed to pay a US$0.25m advance royalty, regardless of production, commencing on the fifth anniversary of the closing date. LIX reserves the right to buy out 1.5% of the 2.5% royalty for a cash payment of US$3m, at any time.
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LIX secured a further 149 claims in consideration for payment to CVL of US$70,500 and has agreed to spend US$0.25m on exploration within two years on 41 of these additional claims.
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Exhibit 4: Location map of Clayton Valley South and North project areas |
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Source: Lithium X Energy |
Clayton Valley South
Lithium X completed its acquisition of the Clayton Valley South project on 25 February 2016 paying US$0.35m and issuing 4m shares to the vendor. The name of the vendor was not stated. In connection with this acquisition, Lithium X also issued a finder’s fee of 295,000 Lithium X shares, which have now passed the expiration holding date (26 June 2016). Raise at least US$3m via a non-brokered private placement.
The Clayton Valley South project covers an area totalling approximately 9,540 acres (3,861 hectares). The property is strategically located between and contiguous with the Silver Peak lithium mine operated by Albemarle Corp. on the northern boundary, the Clayton Valley South project operated by Pure Energy Minerals Ltd to the east and the Neptune property owned by Nevada Sunrise Gold Corporation to the west.
Brine characteristics: Points to consider
An exploration model will be crucial for Lithium X to understand the complex basin characteristics governing brine deposit formation as well as their development. Such a model would include the identification of prospective aquifers as well as structural controls on ground water flow, recharge rates, path ways/conduits and analysis of impurities such as magnesium, iron and sulphur (as sulphate).
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Focus on brines: Brine deposits are the mainstay of global lithium production and are relatively easy to scale up through the addition of more wells and evaporation ponds. They are generally lower grade than hard rock deposits, but far larger in resource size (other than for a small number of clay-based lithium deposits being developed by Bacanora Minerals, Lithium Americas and European Metal Holdings).
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Aquifer assessment: A detailed understanding of the hydrogeological characteristics governing brine deposits is crucial to understanding the quantities that can be economically extracted and, by extension, the size of operation that can be built. The 2011 Rodinia Lithium PEA on Salar de Diablillos contemplated a 15,000tpa LCE operation. This was based on the then current understanding of well flow rates, porosity and the number of aquifers at that time. An operation of this size is comparable to the 17,400tpa LCE plant treating Olaroz brines currently operated by Orocobre (ASX:ORE, ownership: 66.5%).
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Structural controls: Associated with the hydrogeological characteristics of brine deposits are any structural controls that govern ground water flow. This is important to understand such factors as brine recharge rates and whether brines get diluted from large inflows of water.
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Geochemistry: The chemical makeup of brine deposits is assessed beyond the assaying for economic minerals such as the lithium, borates and potash minerals commonly found. The level of impurities such as magnesium, iron and sulphur (as sulphate) requires careful assessment across all areas of the brine field subject to development, with elevated levels having a negative impact on operating costs. Sal de Los Angeles has a significant database of such data, which will be incorporated into the project’s feasibility study. Clayton Valley does not yet have drill data for us to comment on this. Operating costs rise in tandem with contaminant levels.
As can be seen in the following exhibit, Sal de Los Angeles has very favourable levels of magnesium and sulphate relative to lithium. The key magnesium to lithium ratio for Sal de Los Angeles is 3.8, 64% below the simple average for the peer group. The level of sulphates expressed as the SO4/Li ratio in the following exhibit also shows the project to have a very favourable ratio, 52% below the mean and 39% and 53% below Orocobre and Lithium America’s, respectively. The latter is notable as these projects are located in the same region as the Sal de Los Angeles project.
Exhibit 5: Chemistry of South American brine deposits
Deposit |
Operator |
Location |
Deposit type |
Grade Li |
Grade K |
Ratio |
Ratio |
Ratio |
(mg/l) |
(mg/l) |
K/Li |
Mg/Li |
SO4/Li |
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Sal de Los Angeles |
Lithium X |
Argentina |
Na2SO4-K2SO4-Li2SO4 |
501* |
6,206 |
N/A |
3.8 |
14.6 |
Sal de Vida |
Galaxy |
Argentina |
Na2SO4-K2SO4-Li2SO4 |
782 |
8,653 |
11.1 |
2.2 |
11.5 |
Salar de Hombre Muerto |
FMC Corp |
Argentina |
Na2SO4-K2SO4-Li2SO4 |
744 |
7,404 |
10.0 |
1.4 |
13.8 |
Salar de Atacama |
Abermarle (Rockwood)/SQM |
Chile |
Sulpo-Li2S04-LiCl-CaCl2 |
1,835 |
22,626 |
12.3 |
6.4 |
11.0 |
Salar de Olaroz |
Orocobre |
Argentina |
Na2SO4-K2SO4-LiSO4 |
774 |
6,227 |
8.0 |
2.6 |
24.1 |
Salar de Cauchari |
Lithium Americas/SQM |
Argentina |
Na2SO4-K2SO4-LiSO4 |
618 |
5,127 |
8.3 |
2.9 |
30.9 |
Salar de Maricunga |
Li3 |
Chile |
KCl-LiCl-CaCl2 |
1,036 |
8,869 |
8.6 |
8.0 |
1.1 |
Salar de Uyuni |
COMIBOL |
Bolivia |
Sulpo-Li2SO4 |
424 |
8,719 |
20.6 |
18.6 |
24.4 |
Salar de Rincon |
Rincon Lithium |
Argentina |
Sulpo-Li2SO4 |
397 |
7,513 |
18.9 |
8.6 |
30.8 |
West Taijinaier |
Citic |
China |
Sulpo-Li2SO4 |
256 |
8,444 |
33.0 |
61.5 |
137.9 |
Zhabuye Salt Lake |
Unknown |
China |
Li2CO3-Na2SO4 |
1,217 |
17,083 |
14.0 |
0.0 |
32.0 |
Arithmetic average |
808 |
9,716 |
12.0 |
10.5 |
30.2 |
Source: Company websites and Edison Investment Research. Note: *Mean indicated category grade only.
Exhibit 6: Chemistry of Nevada brine deposits
Deposit |
Operator |
Location |
Deposit type |
Grade Li |
Grade K |
Ratio |
Ratio |
Ratio |
(mg/l) |
(mg/l) |
K/Li |
Mg/Li |
SO4/Li |
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Clayton Valley |
Pure Energy |
Nevada |
Na2SO4-K2SO4-Li2SO4 |
102 |
1 |
N/A |
2.0 |
23.0 |
Clayton Valley North |
Lithium X |
Nevada |
Na2SO4-K2SO4-Li2SO4 |
N/A |
N/A |
N/A |
N/A |
N/A |
Clayton Valley South |
Lithium X |
Nevada |
Na2SO4-K2SO4-Li2SO4 |
N/A |
N/A |
N/A |
N/A |
N/A |
Silver Peak |
Albemarle (Rockwood) |
Nevada |
Na2SO4-K2SO4-Li2SO4 |
245 |
5,655 |
23.1 |
1.4 |
30.9 |
Arithmetic average |
174 |
2,828 |
16.3 |
1.7 |
27 |
Source: Company websites and Edison Investment Research
Technical management bolstered by ex-Rockwood CEO
Newly appointed Lithium X COO Eduardo Morales, a past-CEO of Rockwood Latin America before its takeover, has considerable local expertise in the development of brines similar to Los Angeles. Specifically, his expertise involves the development of South America’s first producing lithium carbonate plant. His experience will be invaluable as the company looks to firm up its understanding of the technical aspects of the Sal de Los Angeles project. His responsibilities will include addressing the development characteristics particular to brine deposits, such as:
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Mining: Brine deposits by their very nature cannot be mined by conventional means (ie dig and blast, underground or via open pit). Instead brines require a ‘well field’ to be developed with brines flowing to surface via artesian pressure or, if required, artificially pumped. This naturally places them, including Sal de Los Angeles and Clayton Valley, at the lower end of the global cost-curve for lithium producers.
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Metallurgy: Critical to the production of high-purity lithium products for use in the manufacture of lithium-ion batteries and other high-end technology applications. Levels of impurities must be assessed at the resource definition stage with any impurities (ie magnesium, iron and sulphates) removed. For the benefit of the end user, removal of impurities and the production of large volumes of consistent quality lithium carbonate or lithium hydroxide require the running of a pilot processing plant, such as that currently operated under JV by SESA. See page 4.
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Product sales: Lithium has no openly traded market and the majority of lithium produced is sold via contract with the end user (eg Panasonic, BYD, LG, etc). As such a company’s proven ability to produce consistently high-purity lithium products (as discussed above) is critical to it agreeing supply contracts and guaranteeing revenues.
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Infrastructure – Argentina: The closest producing lithium mine to Sal de Los Angeles is Salar de Hombre Muerto, located 130km to the north. A transfer facility is operated by FMC Corp at nearby Pocitos to handle concentrated Hombre Muerto brines. This operation has access to the La Puna Natural Gas pipeline and also the General Belgrano railroad. The 2011 Rodinia PEA on Salar de Diablillos contemplated a pre-treatment plant on site to produce concentrated brine for further treatment elsewhere, as well as potash for immediate sale. The concentrated brine, or bittern, would then be shipped to a LCE/Borates process facility at Pocitos, potentially allowing for access to the existing La Puna Natural Gas Pipeline and General Belgrano Railroad.
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Infrastructure – Nevada: Clayton Valley North and South are located next to an existing mine, Silver Peak. With the state of Nevada already being the US’s dominant mining region (mostly gold), we would not expect any major obstacle to development from an infrastructure point of view.
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Exhibit 7: Idealised schematic of brine extraction and processing |
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Source: Lithium X corporate presentation. Note: LIX does not currently envisage reinjection of brines from the pond to the salar. |
Rodinia Lithium 2011 Los Diablillos PEA outcome
Below we note the outcome of the 2011 Preliminary Economic Assessment (PEA) on the Sal de Diablillos salar. This PEA, completed by SRK consulting and commissioned by Rodinia Lithium, is subject to revision by Lithium X as it was compiled at a time when lithium demand related as much to its uses in electronic devices such as tablets and smart phones as its uses in electric vehicles. With a step change in demand related to electric vehicle use, which is expected to accelerate, the scope of any pre-development lithium project needs to account for the current and future size of the electric vehicle market.
We also note that the PEA included revenues and costs attributed to the production and sale of boric acid, which we understand will not form part of the feasibility study’s economic analysis.
The PEA contemplated a 15ktpa LCE plant, operating over a 20-year life-of-mine, costing a total of US$120m to develop (with a further US$55m incurred as sustaining capital over life-of-mine). The PEA also assumes production of 52ktpa of potash and 18ktpa of boric acid. Lithium carbonate, potash and boric acid price assumptions were US$5,500/t, US$620/t and US$1,150/t respectively. The estimated average LCE and potash operating costs were US$2,280/t LCE and US$253/t LCE, respectively. Boric acid processing is considered incidental to processing LCE and potash and has no direct cost of production. The total operating cost per LCE tonne on average is therefore US$2,533/t.
After royalties (3% of gross revenues) and taxes (35%) and on the basis of the above data inputs, the 2011 Rodinia-commissioned PEA returned a positive NPV8 of US$560.8m and an internal rate of return of 34%.
We would expect, purely on the basis of current LCE prices and the anticipated future strength of prices for this product alone, that Lithium X’s upcoming economic assessment of this project should exceed that of the historic 2011 SRK authored report. We note from a number of industry sources that lithium carbonate prices are on and off-contract at or above US$10,000/t. However, we caution as to the use of this price over the long term due to risks associated with a lack of future demand driven by a slower than anticipated take up of electric vehicles and the potential for future oversupply. On a per Lithium X share basis, this undiluted and unfinanced PEA NPV8 outcome is worth C$7.57 (US$5.75). This assumes a mine start-up date of 2020. We adjust the capex assumption of US$120m given in the PEA on the basis that it is far too low compared with similar projects in the region and use Orocobre’s US$207m initial capex estimate as given in its 2011 feasibility study on its Salar de Olaroz project as a guide, adjusted to include a contingency amount of US$22.1m, also stated in the 2011 feasibility study. The total US$229.1m capex figure used by Orocobre provides for a 17.5ktpa LCE operation (which is now in production following some further minor capital injections to rectify certain process plant bottlenecks). Further, a 17.5ktpa operation is comparable to the 15.0ktpa operation outlined in the 2011 Diablillos PEA.
Factoring in assumed share dilution based on 50% of our capex assumption of US$229.1m raised in equity at the company’s prevailing share price of C$2.30 results in a ‘post-dilution’ value of C$4.50 (US$3.42) per share (Exhibit 8).
Exhibit 8: Illustrative view of PEA outcome post-dilution (assumes 50% raised in equity)
Parameter |
Unit |
Value |
NPV8 (current money terms) |
US$m |
561 |
Adjusted NPV (assumes 2020 start-up) |
US$m |
383 |
Current LIX shares in issue |
no. (millions) |
66.6 |
Undiluted |
US$ per LIX share |
5.75 |
Total initial capex |
US$m |
229.1 |
50% of capex raised as equity |
US$m |
114.55 |
LIX share price |
US$ |
2.30 |
New shares issued |
no. (millions) |
49.8 |
LIX EV post equity raise |
US$m |
498 |
Total new no. of shares post-equity raise |
no. (millions) |
116.4 |
LIX ownership (assumes farm-in completed) |
% |
80 |
LIX share value post-dilution |
US$ |
3.42 |
Source: Edison Investment Research. Note: Forex rate used: US$0.76/C$.
The above rudimentary analysis of the potential post-dilution value of Sal de Los Angeles cannot factor in future resource expansions or the eventual size of reserve (although we note the current new resource estimate factors in certain parameters that guide to the amount of recoverable brine), the cost of eventual development based on changes to the scope of the PEA or the costs and revenues associated with boric acid production (which may well be excluded, though we note boric acid production is incidental to lithium production). However, it does provide an illustrative order-of-magnitude view of the project’s potential value. It suggests that the level of production achievable from Sal de Los Angeles (based on the hydrogeochemical and hydrogeological characteristics given in the PEA) will warrant a material revaluation of Lithium X’s shares. A feasibility study on the project, which is currently stated to run to at least end 2017, will significantly de-risk the project and provide significantly more robust cost inputs and a far more defined project scope.
Resource qualities, scale, grade and EV/t LCE values
An assessment of EV/t per project is provided in Exhibit 9 and currently shows that, based on the inclusion of the new Sal de Los Angeles inferred and indicated resource, Lithium X ranks in value alongside its regional peer Lithium Americas, yet has only just provided to market a code-compliant resource estimate. We consider Lithium X’s current market valuation reflects confidence by investors in the region in which Diablillos is situated, which is an established lithium-producing area already host to a number of operating lithium brine operations.
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Exhibit 9: EV/t per lithium exploration company |
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Source: Edison Investment Research plus Bloomberg |
Lithium X also has a strong technical management team that brings invaluable knowledge of development brine deposits and, crucially, lithium carbonate plants in South America. Lithium processing is still relatively immature, with pilot plant testing critical to guaranteeing project revenues. There are relatively few processing plants and the recent issues surrounding Orocobre’s ramp up (caused by a number of bottlenecks relating to “physical and equipment limitations and the development of good-working practices”) to full production are an indication of the complexities involved in successfully producing lithium carbonate.
Exhibit 10 provides a visual overview of lithium project resource sizes and grades (given in LCE terms). A general pattern exists in that the generally smaller and higher-grade hard rock deposits group together on the left, with the larger, but lower-grade clay and brine-based deposits situated centre to centre-right. The historical Sal de Los Angeles resource compares very favourably with the lithium grade of its local peers (Salar de Olaroz and Sal de Vida); while its resource size is on the low side compared to its local peers. However, the scale of the Diablillos brine resource is such that it would likely be able to support an appropriately sized (15-20ktpa) lithium operation for a period of greater than 20 years.
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Exhibit 10: Lithium project resource sizes (x-axis and bubble size) and grade in LCE terms (y-axis) |
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Source: Edison Investment Research |
Lithium X Energy: Company history
Lithium X was incorporated in Alberta on 28 August 1997 and moved to British Columbia effective 11 May 2011; it trades under the symbol LIX on the Canadian Venture Exchange. The following bullet points provide a summary of key historical events:
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26 November 2015: Completed its reactivation pursuant to which it acquired the option to acquire a 100% interest in the NSP Lithium Claims in Nevada from Clayton Valley Lithium. The reactivated company name became Lithium X.
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Reactivation followed an amalgamation agreement between the company and registered business 1045564 B.C. Ltd dated 5 November 2015.
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Related to this amalgamation agreement, the company at the time issued 5m shares to shareholders of 1045564 B.C Ltd. Further, the company issued 1m shares to Clayton Valley Lithium and 0.4m shares to a consultant.
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Concurrent with the issue of shares as above, the company completed a private placement of 11,696,669 shares at C$0.15 each for gross proceeds of C$1,754,500 and granted 1,890,000 stock options with exercise periods ranging from three to 10 years at C$0.15.
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24 December 2015: Lithium X completed a non-brokered placement of 10,825,000 shares at C$0.30 each from gross proceeds of C$3,247,500. No options were issued in connection with this raise.
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16 February 2016: Appointed Will Randall, P Geo as the new VP of project development.
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18 March 2016: Completed a non-brokered private placement of 8,332,470 at a price of C$1.02 each for gross proceeds of C$8,499,119. No options were issued in connection with this raise.
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20 April 2016: Lithium X completed its acquisition of an initial 50% interest in Potasio y Litio de Argentina (PLASA), which owns 100% of Sal de Los Angeles, from Aberdeen International. This comprised the issue to Aberdeen of 8m Lithium X ordinary shares. PLASA entered into a JV agreement with Salta Exploraciones for the development of a pilot plant at the project.
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The technical and project management team was significantly strengthened by the addition of Eduardo Morales (announced on 29 June 2016), ex-Rockwood Lithium Latin America CEO, as Lithium X’s new chief operating officer. As per the company’s release, “Mr Morales is an engineer with 36 years of experience who formerly built and operated one of the world’s largest lithium brine operations. As President of Rockwood Lithium Latin America, he successfully led the development, commissioning and operation of Rockwood’s Salar de Atacama project. His tenure with Rockwood Lithium ended with the company’s sale to Albemarle Corporation for US$6.2 billion in 2014.”
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Also appointed to Lithium X’s management team is Andres Barrientos, who has been appointed project general manager of South American operations. As per Lithium X’s announcement dated 29 June 2016, “Mr. Barrientos, a chemical engineer, was the Engineering & Research Superintendent of Rockwood Lithium in Chile until 2012 when he moved to BHP’s Escondida, the world’s largest copper mine. He also helped develop expansion and improvement projects including operational plants for lithium carbonate, lithium chloride and the study of new technologies for the production of lithium hydroxide.”
Financials
At 31 March 2016 Lithium X had C$10.8m in cash. Post-period the company completed, via the issue of 6.1m new shares at C$1.65 each, a non-brokered private placement for a further C$10m (before costs), and C$9.4m (after finder’s fees of C$0.6m). After project and central costs, the company has stated that it currently has “over C$18m cash in-hand” (28 July announcement).
The company forecasts it will spend C$5.5m on Sal de Los Angeles over the coming year. This has already provided for an updated NI 43-101 resource estimate at Sal de Los Angeles, and will fund the completion of a feasibility study and costs incurred with the ponding facility trial (ie C$3.3m, after which Lithium X will own 80% of the project).
The company has budgeted a further C$0.96m to provide an inferred resource estimate for its Clayton Valley project in Nevada and has an annual G&A budget totalling C$1.8m.
Therefore, a total of C$8.3m in expected expenditure can be easily met via the company’s current stated cash resources.
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