Executive Summary

Contents

1        Introduction

2        Key Financial Outcomes of Enhanced Feasibility Study

3        Project Background

4        Enhanced Feasibility Study

5        Project Location 

6        Tenements

7        Geology

8        Resource and Reserve

9        Mining

10      Metallurgy and Test work

11      Process Plant

12      Infrastructure

13      Environmental and Permitting

14      Project Implementation

15      Project Schedule

16      Operating Strategy 

17      Capital Cost Estimate

18      Operating Cost Estimate

19      Market Analysis

20      Financial Analysis 

21      Project Finance

22      Risk

23      Future Programs

 

 

 

1     Introduction

The Tiris Project is a greenfield calcrete uranium project first discovered by Aura Energy in 2008. It represents the first development in a significant new global uranium province in Mauritania with a Mineral Resource Estimate of 59Mlbs U₃O₈ and considerable exploration upside. The mineralisation is naturally suited to low capital cost development and low operating cost extraction of uranium, presenting an opportunity for near term development of the Project.

The Enhanced Feasibility Study assesses the potential to increase U₃O₈ production from that previously reported in the 2021 DFS, following improvements in Mineral Resource confidence with the Mineral Resource Estimate Upgrade announced in February 2023. The assessment has been made utilising incremental addition of modular processing trains based on 2021 Feasibility Study assumptions.

2     Key Financial Outcomes of Enhanced Feasibility Study

 

Key Financial Outcomes	Unit	Enhanced Feasibility Study Mar-23	Definitive Feasibility Study Aug-21
Price Inputs
LOM Average U3O8 Price	US$/lb U3O8	64[5]	60
US$/A$		0.70	0.70
Valuations and Returns
NPV8 (post-tax, real basis, ungeared)	US$M	226	80
IRR (post-tax, real basis, ungeared)	%	28%	22%
Total Project Payback	Years	4.5	3.75
Cashflow Summary
Life of Mine (LOM)	Years	16	15
Uranium Produced (LOM)	Mlbs U3O8	25.5	12.1
Gross revenue (LOM)	US$M	1,562
Free cash-flow (Pre-tax)	US$M	906	420
Free-cash-flow (Post-tax)	US$M	554	265
Unit Operating Cost
All in Cost	US$/lb U3O8	35.6	37.3
All in Sustaining Cost	US$/lb U3O8	28.7	29.8
C1 Cash Cost	US$/lb U3O8	25.2	25.4
Capital Cost
Capital Cost - Start up	US$M	85.8	74.8
Capital Cost - Ramp up	US$M	90.1
Total Development Cost	US$M	175.9	74.8

Table 2‑1 Key Financial outcomes of Enhanced Definitive Feasibility Study

 

 

3     Project Background

The Tiris Project is a greenfield calcrete uranium project first discovered by Aura Energy in 2008. Located in the Sahara Desert in northeast Mauritania it represents the first major calcrete uranium discovery in the region. The Project is 100% owned by Tiris Ressources SARL, which is 85% owned by Aura Energy Ltd and 15% by the Mauritanian Government's Agence Nationale de Recherches Géologiques et du Patrimoine Minier (ANARPAM)

A Scoping Study was completed in 2014. This was updated into a Feasibility Study (FS) document in May 2017, to support an application for exploitation licences. FS and an extensive Environmental and Social Impact Assessment (ESIA) were submitted on 24th May 2017 to the Mauritanian Ministry of Petroleum, Energy and Mines, and formally approved by the Mauritanian Government on 5th October 2017.

A Definitive Feasibility Study (DFS) for a 1.25 Mtpa mine and process plant was completed in 2019 has been designed to take full advantage of these unusual characteristics, whilst providing a low capital cost and rapid project development and construction. The Capital Estimate for the DFS was updated in August 2021

Exploitation licences (2491C4 and 2492C4) for the Ain Sder and Oued El Foude permits were granted on the 8^th of February 2019[6] and Mining Conventions for these permits were signed in January 2023.

4     Enhanced Feasibility Study

The Enhanced Feasibility Study (EFS) represents an incremental assessment of the potential to increase production rates for the Tiris Project to fully utilise the updated Ore Reserve Estimate as reported in this announcement and the 2023 Mineral Resource Estimate (MRE) update[7]. To achieve this Aura has made the following assumptions:

·    All inputs to EFS based on Definitive Feasibility Study 2021[8]

·    Process throughput increased based on the addition of modular units defined in DFS.

·    Ore Reserve Estimate updated based on 2023 Mineral Resource Estimate Upgrade

·    Mining schedule and costs updated to be based on updated Ore Reserve Estimate.

·    Capital Estimate escalated by 15% for inflation pending completion of FEED study, Q4 CY 2023.

·    Mining and reagent costs updated.

·    U₃O₈ pricing assumptions updated to reflect a structural shift in the uranium market.

 

 

5          Project Location

Tiris uranium project located 680km from Zouérat and 1,400km from Nouakchott, Mauritania's Capital.

Figure 5‑1

Figure 5‑2: Location of the Tiris Uranium Project in Mauritania

Mauritania is a country with a well-established and sizeable mining industry and a favourable and well-administered Mining Act. The Government is stable, democratic, based on the French civil law system and supportive of foreign investment. It has an established reputation for maintaining stability and security within its borders.

The predominant spoken languages in Mauritania are Hassaniya, Arabic, Pulaar, Soninke, Wolof and French (widely used in the media and among educated classes). Modern Standard Arabic is the official language.

As of 2018, Mauritania had a population of approximately 4.5 million. The local population is divided into three main ethnic groups: Bidhan, Haratin, and West Africans. Mauritania is nearly 100% Muslim with most inhabitants adhering to the Sunni denomination. The Sufi orders, the Tijaniyah and the Qadiriyyah have great influence in the country. Mauritania gained its independence from France on 28 November 1960, after 59 years of French colonialism. Mauritania held its first democratic presidential elections in 2007 and again in 2009 after a coup. The outgoing president, Abdel Aziz, held power from 2009 for the regulatory two terms, and gained widespread international and internal support. Abdel Aziz's Defence Minister has just been elected as the new President in June 2019.

6          Tenements

The Project is 100% owned by Tiris Ressources SARL, which is 85% owned by Aura Energy Ltd and 15% by the Mauritanian Government's Agence Nationale de Recherches Géologiques et du Patrimoine Minier (ANARPAM).

The key approvals provided for the Tiris project to date are:-

·    Mining Exploitation licences (2491C4 and 2492C4) granted for the two Eastern Resource zones at Oued El Foule and Ain Sder on February 8th, 2019

·    Environmental and Social Impact Assessment (ESIA), approved on 5th October, 2017[9].

·    Mining Conventions for 2491C4 and 2492C4 Licences, signed January 2023

Once the project go-ahead is given and design is resolved, additional approvals will include:-

·    Construction permit for any construction work outside Aura's mining leases.

·    Water approval permit to draw water.

·    Road usage permit for any roads to be constructed outside Aura's mining leases.

·    Import permit for relief of Customs and import duties on all imported materials.

·    Re-certification of existing Shield airstrip

·    Power permit to establish three power generation plants.

·    Health permit to establish a first aid clinic on site.

·    Labour permit to approve Aura's Mauritanisation plan to train local personnel and replace expatriates.

·    Prior authorisation for production and export of Uranium Oxide Concentrate

7          Geology

·    Mineralised gravels and weathered granite occur at surface, or under a very thin (<30cm) veneer of wind-blown sand.

·    Uranium mineralisation occurs principally as carnotite K₂(UO₂)₂(VO₄)₂.3H₂O.

·      Carnotite occurs as fine dustings and coatings on granite or granite mineral fragments.

The Tiris resources lie in the north-eastern part of the Reguibat Craton, an Archaean (>2.5 Ga) and Lower Proterozoic (1.6-2.5 Ga) aged complex composed principally of granitoids, meta-sediments and meta-volcanics. The resources lie within Proterozoic portions of the craton. This part of the craton generally consists of intrusive and high-grade metamorphic rocks of amphibolite facies grade.

Several small uranium vein deposits were known in the Reguibat Craton from exploration during the 1950's pointing to the existence of a poorly explored uranium province. Economically significant calcrete-type uranium deposits had not been reported in Mauritania prior to Aura's discoveries.

 

7.1      

7.2       Local Geology

In Aura's resource zones, the underlying rocks are pre-dominantly granitic and of two main types:

·    Pale grey medium-grained granite and granodiorite with coarse phenocrysts of plagioclase, generally unfoliated and forming low smooth outcrops. The uranium content is low, typically 1 to 2 ppm

·    Finer-grained red to pink porphyritic granite, less abundant than the grey granite. This granite typically has higher uranium content in the range 5 to 20 ppm and is therefore a moderately 'hot' granite. The red granite is typically fractured and foliated and is believed to have formed by alteration of the grey granites in zones of deformation.

All the resource zones lie beneath very flat land surfaces covered by surficial hamada and thin aeolian sand deposits. These largely cover the basement rocks, which appear only as scattered outcrops.

7.3       Mineralisation

The uranium resources lie predominantly within either weathered, partially decomposed red granite or in colluvial gravels developed on or near to red granites. The resources are believed to have developed within shallow depressions or basins, where colluvial material has accumulated in desert sheet wash events.

Calcrete-hosted uranium mineralisation of several metres in thickness occurs in gravels and weathered granite at surface to a depth of 8 metres, or under a very thin (<30cm) veneer of wind-blown sand. The weathered veneer of relatively unconsolidated material that overlies fresh rock is typically less than 5 metres in thickness, although locally it can occur up to 12 m depth.

The mineralised bodies form laterally continuous, single, thin sheets overlying fresh rock, usually granite. This offers the opportunity for easy, low-cost mining and little or no crushing.

Uranium mineralisation occurs principally as carnotite K₂(UO₂)₂(VO₄)₂.3H₂O, occurring as fine dustings and coatings on granite or granite mineral fragments usually mixed with white powdery calcium carbonate. The carnotite grain size is mostly ultrafine micron scale. The deposits appear to have formed by near-surface leaching of uranium from the uraniferous red granites by saline groundwaters during the wet Saharan "pluvial" periods. There have been many of these periods over the past 2.5 million years, the most recent ending only 5,900 years ago. Evaporation during the subsequent arid periods caused the precipitation of the uranium vanadates, along with calcium, sodium and strontium carbonates, sulphates and chlorides.

8          Resource and Reserve

8.1       Resources

This Feasibility Study is based upon consolidated Mineral Resources reported in the ASX announcement entitled "Major Resource Upgrade at Aura Energy's Tiris Project" released on 14^th February 2023 and available to download from asx.com.au ASX:AEE. In that report, Measured and Indicated Resources were listed at 62.1 Mt of ore for 29.6 Mlbs U3O8, at 216 ppm. The combined Mineral Resources Estimate, including an Inferred Resource Estimate, is 113Mt of ore at 236 ppm for 58.9 Mlbs U₃O₈. All resources were reported at a 100ppm grade cut-off

 

 

Area1, 2	Class	Tonnes (Mt)	U3O8      (ppm)	U3O8    (Mkg)	U3O8    (Mlb)
Hippolyte North	Measured	8.0	236	1.9	4.2
	Indicated	5.8	217	1.3	2.8
	Inferred	4.7	212	1.0	2.2
	Sub-Total	18.5	224	4.1	9.1
Hippolyte Marie & West	Inferred	8.2	310	2.5	5.6
Hippolyte South	Indicated	4.6	192	0.9	2.0
	Inferred	2.7	176	0.5	1.1
	Sub-Total	7.4	186	1.4	3.0
Lazare North	Measured	1.0	282	0.3	0.6
	Indicated	10.1	229	2.3	5.1
	Inferred	3.7	210	0.8	1.7
	Sub-Total	14.8	228	3.4	7.4
Lazare South	Measured	8.6	233	2.0	4.4
	Indicated	5.2	226	1.2	2.6
	Inferred	4.8	222	1.1	2.3
	Sub-Total	18.6	228	4.2	9.3
Sadi	Measured	11.5	189	2.2	4.8
	Indicated	7.4	200	1.5	3.2
	Inferred	10.3	228	2.4	5.2
	Sub-Total	29.2	206	6.0	13.2
All Deposits	Measured	29.1	218	6.4	14.0
	Indicated	33.0	215	7.1	15.6
	Inferred	34.5	237	8.2	18.0
Total Tiris East		96.6	224	21.6	47.7
Oum Ferkik	Inferred	16.4	305	5.1	11.2
Total Aura Resources		113.0	236	26.7	58.9

Table 8‑1 - 2023 Mineral Resource Estimate

¹ The information in this announcement is extracted from ASX announcement entitled "Major Resource Upgrade at Aura Energy's Tiris Project" released on 14^th February 2023 and available to download from asx.com.au ASX:AEE. The Company is not aware of any new information or data that materially affects the information included in the original market announcement and, in the case of estimates of Mineral Resources that all material assumptions and technical parameters underpinning the estimates in the relevant market announcement continue to apply and have not materially changed. The Company confirms that the form and context in which the Competent Person's findings are presented have not been materially modified from the original market announcement.

 

² This Tiris Resource Inventory aggregates the 2023 Mineral Resource Estimates by H&S Consultants Pty Ltd on the Lazare North, Lazare South, Hippolyte, and Hippolyte South deposits and the 2011 Mineral Resource Estimates by Coffey Mining on the Sadi, Ferkik West, Ferkik East, Hippolyte West and Marie deposits. The 2011 Resource Estimate was the subject of Aura ASX announcement dated 19 July, 2011 "First Uranium Resource in Mauritania". The 2011 Mineral Resource Estimate was produced in compliance with the 2004 edition of the 'Australasian Code for Reporting of Exploration Results, Mineral Resources and Ore Reserves'. Aura confirms that all material assumptions and technical parameters underpinning the 2011 Mineral Resource Estimates in the relevant market announcement continue to apply and have not materially changed.

8.2       Reserve Estimate

 

8.2.1     Mining Block Models

The mining block models were supplied as regularized, diluted models by Aura Energy as Multiple Indicator Kriged (MIK) with a panel size of 50 mE x 50 mN x 1.0 mRL.  This block size represents an appropriate Selective Mining Unit (SMU) block size for the assumed mining methods of the ore/waste contact and underlying ore zones and is unchanged from the 2019 Study.

Updated models were provided for Lazare North, Sadi and Hippolyte Zone 3. All other areas were unchanged from the 2019 Study.

8.2.2     Cut Off Grade

Aura Energy provided an updated cost structure for the project which included an increased production rate and associated recoveries, as summarised in Table 8‑2:

 

Description	Unit	Value
Labour, Administration, FIFO.	US$/lb	$1.63
Diesel Generator Maintenance	US$/lb	$0.19
Contract Mining	US$/lb	$7.07
Road Maintenance	US$/lb	$0.18
Process Operating & Reagent	US$/lb	$3.32
Spares	US$/lb	$1.15
Transport Costs	US$/lb	$2.27
Tailings/Reject Management	US$/lb	$0.77
Medical Clinic labour	US$/lb	$0.15
Camp Management	US$/lb	$0.88
Solar	US$/lb	$0.26
Diesel Costs	US$/lb	$3.48
Communications	US$/lb	$0.03
Radiation Management.	US$/lb	$0.08
External Services	US$/lb	$0.01
Total	US$/lb	$21.70

Table 8‑2 - Preliminary Operating Costs

 

Removing the contract mining cost the preliminary non-mining operating cost is US$ 14.63 /lb

Based on preliminary production targets for mining studies this resulted in a preliminary non-mining cost of US$9.62/t mill feed.

At this cost, and a planned recovery of 83.1% the cut-off grades, at various selling process is shown in Table 8‑3

 

Selling Price (US$/lb)	Cut-Off Grade (ppm)
$40	131
$50	105
$60	87
$70	75

Table 8‑3 - Cut Off Grades

Aura undertook market research into the projected sales price and came to the recommendations that a reasonable price to use for the study is $60 per lb U3O8 in 2022 real terms. Aura's recommendation was summarised as;

A number of industry and financial market commentators have provided estimates of future pricing based on incentive curves. Equity analyst consensus for uranium prices in the late 2020s and into the 2030s sits in the range of $55 to $60 per lb.

The current TradeTech long term market price indicator, as published for the end of November 2022, is $53.00 per lb U3O8. TradeTech's production cost indicator, intended to give an idea of a uranium mine incentive price today, is $56.20.

TradeTech's 2022 market study offers two long term price scenarios, FAM 1 based on a 'risk off' approach where published production target volumes are readily achieved, and FAM 2 based on a 'risk on' approach where there is a reduction in production volumes of 129,000 tU / 15,240 t / 336M lbs between 2020 and 2040. FAM 1 has a midpoint forecast price of $54 per lb and FAM 2 has a midpoint forecast price of $69 per lb in real terms from 2030.  The mean of the two forecasts is $61.50.

Allowing for the preliminary nature of the non-mining costs and the range of uranium pricing a cut-off grade of 110ppm was selected for the study, however, to ensure that the resultant grade within the shells is high enough to achieve the target annual production optimisations were also completed at 125ppm, 150ppm and 175ppm.

 

8.2.3     Mineral Resource Summaries

At a cut-off grade of 110ppm, the total available resource for the study is 59.3 Mt @ 230ppm containing 30.1 Mlbs. This grade is too low to achieve the annual production target of 2.5 Mlbs at the expected milling rates and recoveries. At a cut-off grade of 150ppm the average grade rises to 250ppm and at 175ppm cut-off grade the average resource grade is 313ppm

The resources available for the study, at the various cut off grades are summarised by area in Table 8‑4 to Table 8‑7.

Table 8‑4 - Resource Summary (110ppm CoG)

Mining Area	Measured & Indicated
	(Mt)	(ppm)	(Mlb)
Lazare South	12.4	245	6.7
Lazare North	10.3	245	5.6
Sadi	18.2	209	8.4
Hippolyte Zone 3	4.2	264	2.4
Hippolyte North	9.9	234	5.1
Hippolyte South	4.3	201	1.9
Total	59.3	230	30.1

 

Table 8‑5 - Resource Summary (125ppm CoG)

Mining Area	Measured & Indicated
	(Mt)	(ppm)	(Mlb)
Lazare South	10.7	265	6.2
Lazare North	9.1	261	5.2
Sadi	14.8	230	7.5
Hippolyte Zone 3	3.6	286	2.3
Hippolyte North	8.6	252	4.8
Hippolyte South	3.7	214	1.7
Total	50.5	250	27.8

 

Table 8‑6 - Resource Summary (150ppm CoG)

Mining Area	Measured & Indicated
	(Mt)	(ppm)	(Mlb)
Lazare South	8.7	294	5.7
Lazare North	7.4	290	4.7
Sadi	10.9	263	6.3
Hippolyte Zone 3	2.9	322	2.1
Hippolyte North	6.8	283	4.2
Hippolyte South	2.8	238	1.5
Total	39.6	281	24.5

 

Table 8‑7 - Resource Summary (175ppm CoG)

Mining Area	Measured & Indicated
	(Mt)	(ppm)	(Mlb)
Lazare South	7.1	323	5.1
Lazare North	6.0	319	4.2
Sadi	8.1	298	5.3
Hippolyte Zone 3	2.4	358	1.9
Hippolyte North	5.4	314	3.7
Hippolyte South	2.1	264	1.2
Total	31.1	313	21.5

 

The Ore Reserve Estimate was generated by Resolve Mining Services (Resolve). The overall project financial model was prepared by Aura using inputs from the mining schedule physicals and the cost model. Detailed processing, tailings disposal, power, water, camp infrastructure and logistics, and other costs were also developed as part of the Feasibility Study. Resolve reviewed the cash flow model with Aura to ensure that the project has a positive cash flow outcome, and this has been confirmed.

The declared Ore Reserve Estimate, at a 110 ppm U₃O₈ cut off is shown in Table 8‑8.

Description	Mt	U3O8 (ppm)	U3O8 (Mlb)
Lazare North
Proved	0.9	298	0.6
Probable	7.9	251	4.4
Lazare South
Proved	6.5	264	3.8
Probable	2.6	291	1.7
Hippolyte
Proved	5.7	270	3.4
Probable	7.1	231	3.6
Sadi
Proved	6.1	232	3.1
Probable	3.3	261	1.9
Total Ore Reserve
Proved	19.3	257	11.0
Probable	21.3	251	11.6
Total Tiris East Reserve	40.3	254	22.6

Table 8‑8: Updated Ore Reserve Estimate

Ore Reserves are a subset of Mineral Resources.

                         Ore Reserves conform with and use the JORC Code 2012 definitions.

                         Ore Reserves are calculated using a uranium price of US$65 /lb.

                         Ore Reserves are calculated using a cut-off grade of 110 ppm U₃O₈.

                         Tonnages are reported including mining dilution

                         All figures are rounded to reflect appropriate levels of confidence which may result in apparent errors of summation.

The Ore Reserve Estimate was generated from the Mineral Resource Estimate produced by H&S Consultants (Sydney) with the appropriate modifying factors to apply for mining dilution. This Mineral Resource model was used in an open pit optimisation process to produce a range of pit areas using operating costs and other inputs derived from previous studies. Mining costs were built up from estimates derived from equipment supplier and mining contractor submissions and applied to a detailed mine schedule.

The Ore Reserve Estimate is based on information compiled by the following:

·    Revenue prices, based on historical averages and forward estimates, based on Offtake Agreement with Curzon Resources provided by Aura.

·    Processing recoveries based on the geometallurgical model developed by Aura.

·    Mineral Resource estimate, H&S Consultants, 14 February 2023.

·    Pit optimisation, mine design, production scheduling and mining cost estimation completed by Resolve.

·    Capital costs, Mincore, Simulus Engineers, Adelaide Control Engineers (ACE) and Aura.

·    Operating costs, Mincore, Simulus Engineers, ACE, Mining Plus and Aura.

9          Mining

 

·    The EFS mine schedule supports 15 years production at average 2.0 Mlbs of U₃O₈ per annum, after ramp-up.

·    Mining is free-digging and at surface.

·    Owner mining employed.

Resolve Mining Consultants (Resolve) was commissioned by Aura Energy in November 2022, to complete the mining design for the project, including Ore Reserve estimation in accordance with JORC (2012 Edition) requirements.

The detailed tasks undertaken were:

·    Preliminary mine planning for preparation of information pack to obtain Mining Contractor Pricing.

·    Obtain Mining Contractor pricing and review submissions.

·    Complete pit optimisation including Measured, Indicated, and Inferred (MII) mineral resources for the Lazare North, Lazare South, Hippolyte North, Hippolyte South, Hippolyte Z3 and Sadi Resources as potential mineral inventory.

·    Define mining method and cycle based on optimised pit designs.

·    Develop life-of-mine and mill production schedules including backfilling of beneficiation circuit reject and process tailings.

·    Estimate Ore Reserves and report in accordance with JORC (2012 Edition).

In January 2023 Mining Plus was engaged to complete an owner mining cost model to support the mine schedule.

The uranium mineralisation largely lies within 3 to 5 metres of the surface in a relatively soft, free-digging material containing patchy calcrete. Based on trenching and metallurgical test work to date, this does not require blasting before mining, or crushing prior to beneficiation.

The Enhanced Feasibility Study has shown that the three mining hubs can be developed in a practical sequence to produce 1.7 -2.3 Mlbs/yr UOC through the processing plant for over ten years. The first nine years are from currently defined Measured or Indicated Mineral Resources, which form the declared Ore Reserve Estimate. The total mining cost to develop and operate the mine for 17 years, has been estimated at US$190 million or US$2.14/tonne of material mined. This includes both fixed and variable operating costs, but excludes any capital spent prior to mobilisation.

9.1       Pit Optimisation

Optimization's for the study were completed using the rates from both the 2019 results and the higher average mining costs which will show the impact of increasing mining costs on the potential Ore Reserve.

The optimisation results for the six mining areas, two mining costs and four cut off grades and US$60/lb are summarised in Table 9‑1.

The tables show that over 75% of the total resource falls within the optimisation shells at $60/lb, even at the higher mining costs.

 

 

Mining Area	Mill Feed (Mt)	Mill Feed (ppm)	Mill Feed (Mlbs)	Waste (Mt)	Total (Mt)	Cash Flow (M$)	Cost (US$/lb)	Resource (%)
Lazare South	9.1	272	5.4	10.5	19.6	$94	$35.3	81%
Lazare North	9.2	254	5.2	9.0	18.2	$108	$34.7	93%
Sadi	10.5	245	5.7	11.5	22.1	$84	$38.6	68%
Hippolyte Zone 3	3.2	296	2.1	4.0	7.1	$46	$32.9	85%
Hippolyte North	7.0	244	3.7	7.3	14.3	$72	$36.8	73%
Hippolyte South	3.6	210	1.7	10.7	14.3	$27	$41.0	89%
Total	42.5	253	23.8	53.1	95.6	$430	$36.4	79%

Table 9‑1 - Higher Cost Optimisation Results at 110 ppm COG

The optimisation results show an increase in the mill feed grade as either the cut-off grade increases, or the cost does. At the lowest cost and lowest cut-off grade the average grade mined is 246ppm, this average grade would only produce 1.7 Mlbs pa, and adding a fourth beneficiation train would be required to approach the target of 2.5 Mlbs pa.

Increasing the cut-off grade to 175ppm increases the life of mine average grade to 324ppm, and with this the production would increase to 2.2 Mlbs pa for three trains or 3.0 Mlbs pa from four. The small increase in grade from the higher mining costs will allow more than 3.0 Mlbs pa to be achieved, one average, from all deposits except Hippolyte South using four beneficiation trains.

The tables show that increasing the mining cost only decreases the potential mill feed by less than 10%, and the contained metal within this feed by only 5%. This indicates that the ore being dropped at the higher cost is not significant and the grade associated with this material is at the lower end of that being selected for mining. The drop in waste and therefore total movement is more significant at 15%-20% which does carry through to higher cash flows.

These increased grades, along with the potential need to add a fourth beneficiation train to the processing will decrease the overall mine life. The mine life ranges from over twelve years to less than six for the highest grade with highest throughputs.

 

Beneficiation Trains	CoG (ppm)	Mill Feed (Mt)	Mill Feed (ppm)	Product (Mlbs pa)	Mine Life (yrs.)
3	110	46.8	246	1.7	12.5
3	125	41.2	263	1.8	11.0
3	150	33.1	293	2.0	8.8
3	175	26.3	324	2.2	7.0
4	110	46.8	246	2.3	9.4
4	125	41.2	263	2.4	8.2
4	150	33.1	293	2.7	6.6
4	175	26.3	324	3.0	5.3

Table 9‑2 - Mine Life Comparisons.  Highlighted case (4 beneficiation trains at 110ppm cut off) represents proposed Base Case.

9.2       Pit Shells

The pit shells for the three mining areas are shown in Figure 9‑1 to Figure 9‑5. The figures show the four cut-off grade results as;

100ppm; green

125ppm; blue

150ppm; yellow, and

175ppm; red

In most areas the four shells over lie each other and the difference in inventory is due to the proportion of above cut-off grade material in each model block. The model blocks that fall outside the shells generally have less than 10% mineralization and are uneconomic.

 

 

3.0 km

Figure 9‑1 - Lazare South Optimisation Shells

 

1.5 km

Figure 9‑2 - Lazare North Optimisation Shells

 

 

 

3.0 km

Figure 9‑3 - Sadi Optimisation Shells

 

Figure 9‑4 - Hippolyte North (inc Z3) Optimisation Shells

Figure 9‑5 - Hippolyte South Optimisation Shells

 

9.3       Mine Design

9.3.1     Open Pit Designs

Due to the shallow nature of the deposit and that the optimisations can be used to determine the extent of mining no individual pit designs are required for the study. As the project develops the pit designs will need to be developed but they will still be relatively simple shapes used to extract the ore and waste.

For the study the optimisations shells were cleaned to remove any small un-mineable shapes, and then these clean surfaces coded into the mining model. The blocks within the mining model are 50m x 50m which while is a mineable size a mine panel size of 200m x 200m was selected as the minimum dimensions of each pit. The mining model blocks and mine panels for Lazare South are shown in Figure 9‑6 to indicate the selected minimum pit size.

This pit size was selected as it provides sufficient length on any side to ensure a ramp can be installed and that mine development can be advanced enough for continuous backfilling.

                                 Figure 9‑6 - Lazare South Measured and Indicated Mining Model and Mine Panels

 

9.3.2     Waste Dumps

 

Prior to backfilling being possible each project area will require a waste dump to store the overburden, beneficiation rejects and dry-stacked tailings until sufficient void space has been mined. The size and location of these dumps is determined by the production schedule.

Each dump constructed will be rehandled back into the mining void prior to a mining area being completed.

9.3.3     Mining Method and Cycle

Figure 9‑7: Mining Method, Ore Haulage Circuit

 

A conventional open pit dry mining method, utilising a combination of bulldozers, excavators and trucks will be employed. Mining is anticipated to follow a strip-mining philosophy, where any waste mined will be returned to a previously mined area without the need for building waste dumps or rehandling. It is planned that initial ex-pit dumps or berms will be utilised as the open pit develops, but these should be located immediately adjacent to a pit. The waste material should be able to be simply pushed in when space is available in the mined-out void.

No drilling or blasting is required based on Aura's site investigations and material properties. However, each mining area will require grade control drilling prior to excavation. It is expected that this grade control will be undertaken by either excavator dug pits or a rock saw, which could then be gamma logged to ascertain the in-situ grade.

Stage	Description
Sand Clearing	Any overlying sand is pushed into windrow stockpiles alongside the pit with a bulldozer. Where required these shall be formed as berms to avoid any flooding of the pit from the infrequent rainfall and surface water eventuating.
Overburden Removal	Any overburden is removed by bulldozer onto windrow stockpiles.
Ore and Waste Mining	The ore exposed and associated waste is mined by hydraulic shovel or bulldozer and front-end loader and loaded into haul trucks. The ore is hauled directly to the apron feeder area, whereas the waste is placed into stockpiles alongside the pit unless sufficient mining voids are available for backfilling
Backfilling	When sufficient void volume is available, the mined-out cell is filled with filter pressed process plant tailings, barren rejects discharged from the screening plant and mine waste.
Surface Rehabilitation	Overburden and stockpiled mine waste is pushed over the consolidated cell from the windrow stockpiles at the side of the pit.

Table 9‑3 - Mining Cycle Description

 

9.4       Mine Schedule

Mine scheduling was completed with the following constraints:

The base case target mining rate of 4.18 Mtpa.

·    A plus 10-year project life

·    Measured and Indicated Mineral Resources with minor Inferred Mineral Resources

·    Two years ramp up phase at mining rate of 1.25Mtpa

·    No ore stockpiling

The schedule was completed monthly then summarised annually. Allowances for feed hopper relocations were included between mining areas when a shutdown of the plant and mine occurred.

Ore and waste mining occur concurrently as the ore is defined as a proportion of each resource block, with the remainder being waste. Ore is mined at exactly the processing rate required as there is no stockpiling of ore at the hopper. No advance waste mining occurs.

The mining panels were sequenced from highest value within each mining area before a feed hopper relocation occurs. The operating mine area is grouped into three mining hubs based on their locality and synergies to share resources and available infrastructure. The list of selected mining hubs is summarised in Table 9‑4.

Mining Hub	Open Pits
Lazare Mining Hub	Lazare South Lazare North
Hippolyte Mining Hub	Hippolyte Z3 Hippolyte South Hippolyte North
Sadi Mining Hub	Sadi South Sadi North

Table 9‑4: Resource distribution by mining hubs

 

The final base case sequence has been presented in Figure 9‑8. From Year 4 there will be 3 modular beneficiation circuits available, allowing simultaneous mining at multiple resources.

 

 

Figure 9‑8: Mine schedule ore profile by area. Including grade profile across LOM.

There is a low level of geological confidence associated with Inferred Resources and there is no certainty that further exploration or evaluation work will result in the determination of Indicated Resources or that the production targets reported in this announcement will be realised. The Company confirms that the use of Inferred Resources is not a determining factor to the Tiris Project's economic viability

 

Figure 9‑9 presents the U₃O₈ grade profile as mined and for leach feed.

 

Figure 9‑9: Mined grade profile and leach feed grade profile across LOM. Screen cut size for beneficiation at 150µm for ramp up, reduced to 75µm for operations.

 

The base case ore profile by Mineral Resource confidence is presented in Figure 9‑10. This demonstrates no Inferred material through the ramp up period and no more than 10% Inferred material in the first 5 years through the payback period. Over the LOM 21.04% of mined material was from the Inferred category. The project remains economically viable without the inclusion of Inferred Resource Estimates.

 

 

Figure 9‑10: Ore profile by Ore Reserve and Mineral Resource confidence.

There is a low level of geological confidence associated with Inferred Resources and there is no certainty that further exploration or evaluation work will result in the determination of Indicated Resources or that the production targets reported in this announcement will be realised. The Company confirms that the use of Inferred Resources is not a determining factor to the Tiris Project's economic viability

 

Figure 9‑11 shows the material movement in the start-up and operational phases, along with the strip ratio across the schedule. The average strip ratio (W:O) across the 16-year LOM was 0.79.

Figure 9‑11: Material movement between ramp up stage and operations, with strip ratio.

There is a low level of geological confidence associated with Inferred Resources and there is no certainty that further exploration or evaluation work will result in the determination of Indicated Resources or that the production targets reported in this announcement will be realised. The Company confirms that the use of Inferred Resources is not a determining factor to the Tiris Project's economic viability

 

9.4.1     Upside Scenario

A scenario examining the potential for extension of the project life using additional material from the Inferred Mineral classification was developed.  For this scenario it was assumed that Inferred material could convert to Measured and Indicated Mineral classification along the same parameters observed for the Maiden Ore Reserve Estimate and in the 2022 Resource upgrade program.  In these programs an average of 65% Inferred Resource material converted to Measured and/or Indicated Resource classifications.

The production profile estimated for the upside scenario can be seen in Figure 9‑12.  In this scenario 53.2Mt of material at 110ppm cut off and average grade of 257ppm U₃O₈ was estimated to be mined over 15-year LOM.

 

 

 

Figure 9‑12 - Material profile and grade by Reserve and Resource category for upside scenario.

The upside scenario production profile is based on a Mineral Resources Estimate in accordance with JORC guidelines 2012 (ASX: Major Resource Upgrade at Aura Energy's Tiris Project dated 14 February 2023).  The Company advises that the EFS uses a portion of Inferred Resources; in the first 6 years (less than 10%) and over the 15-year life of mine (24.6%). The Company confirms that the use of Inferred Resources is not a determining factor to the Tiris Project's economic viability.

There is a low level of geological confidence associated with Inferred Resources and there is no certainty that further exploration or evaluation work will result in the determination of Indicated Resources or that the production targets reported in this announcement will be realised.

 

10        Metallurgy and Test work

Process development for the Tiris Project was based on detailed material characterisation. This included detailed mineralogical characterisation early in the project development, supported by various diagnostic techniques.

The results of material characterisation were assessed against established uranium processing options. This allowed early assessment of viable options and rejection of unsuitable options. The primary characteristics driving process selection were defined as:

·    Presence of uranium exclusively with carnotite group minerals.

·    Fine grained nature of carnotite, which could be easily liberated from host particles.

·    Dominance of carbonate minerals over sulphate minerals.

·    Tendency for carbonate minerals to upgrade with uranium, while sulphate minerals were rejected.

·    Presence of swelling and non-swelling clay minerals.

The uranium mineralisation at Tiris occurs principally as carnotite K₂(UO₂)₂(VO₄)₂.3H₂O) and possibly some of the chemically-similar calcium uranium vanadate, tyuyamunite Ca(UO₂)₂(VO₄)_2.5-8H₂O) in varying proportions.

Carnotite is a radioactive, bright-yellow, soft and earthy vanadium mineral that is an important source of uranium. A hydrated vanadate, pure carnotite contains about 53 % uranium, 12 % vanadium, and trace amounts of radium. It is of secondary origin, having been formed by alteration of primary uranium-vanadium minerals. It occurs chiefly with(its) in, locally as small pure masses, particularly around fossil wood.

The Carnotite grain size for the Tiris material is in the range of 5-15µm diameter across the deposits. The majority of carnotite grains identified were within the micron size range.

Several Ore Domains were defined by geometallurgical modelling based on process behaviour. These Domains were defined by gangue mineralisation and particle size distribution. Geometallurgical modelling focused on the first 4 years of mine production (payback period), for the Lazare North and Lazare South Resources. The geometallurgical modelling covered 18% of defined Ore Reserves for the EFS mine schedule, with additional work planned through the FEED study.

The primary differentiating factors for the Ore Domains were:

·    Proportion of mass distribution reporting to -75µm screen fraction.

·    Proportion of sulphate mineral reporting to -75µm screen fraction.

·    Upgrade factor of uranium to -75µm screen fraction

The material characterisation identified that the most appropriate process flowsheet would include ore beneficiation, followed by a heated alkaline leach, concentration of leached uranium and precipitation of yellowcake product.

To investigate the technical viability of process flowsheet options a steady state simulation model was developed. This allowed rapid assessment of process configurations and early rejection of options that were technically unsuitable. The steady state simulation model was used throughout process development test work to support test work results and allow for solution recycle and potential impurity build up at every stage. This allowed test work programs to be developed that were targeted specifically at design critical parameters.

10.1     Ore beneficiation

There is a high portion of barren sands within the mineralised calcrete. Removal of the sand prior to leaching reduces the throughput in the hydrometallurgical process plant, with a subsequent reduction in capital and operating costs. The Tiris mineralisation is particularly well suited to this type of ore beneficiation.

The uranium bearing carnotite is very fine grained, with average particle diameter of 5-15µm. The carnotite, clay minerals and fine-grained calcite is loosely bound to barren silica and sulphate rich gravels. This can be easily separated using low power washing in a rotary scrubber, resulting in concentration of carnotite in the fine fractions. Uranium can be separated in these fine fractions using simple screening, resulting in recovery of over 90% of the uranium into between 10% and 15% of the total mass, as demonstrated in Figure 10‑1.

The response to ore beneficiation allows rejection of most of the ore mass, greatly reducing the throughput to leaching. This translates to Capital savings through requirement for a significantly smaller leach circuit, along with significant operating savings through reduction in reagent consumption.

Beneficiation test work was undertaken at AMML, Gosford on ~100kg domain composite samples. This included benchtop scrubbing of bulk samples followed by screening to 150µm to product ore concentrates of 10-15kg for each Domain Composite. These provided the inputs for development hydrometallurgical test work at ANSTO Minerals.

Bulk Domain Composite samples were also prepared at Mintek, South Africa. These samples were scrubbed in a 1m diameter rotary scrubber and screened at 150um on an industrial scale single deck Derrick Stack Sizer. Technical support for Derrick screening test work was provided by Derrick International.[10]

Figure 10‑1: Mass recovery, uranium recovery and product uranium grade for screen cut size of 150µm. All composites.

 

 

 

 

 

 

 

 

 

 

10.2     Alkaline Leaching

The nature of the carnotite mineralisation also translates to improved leaching response. A program of bulk heated alkaline leaches was undertaken at ANSTO Minerals. Figure 10‑3 shows the leaching profile by Domain composite for Lazare North and Lazare South. The fine-grained nature of carnotite results in very rapid leaching, with the reaction essentially complete within 8 hours. This is significantly faster than leaching rates for similar calcrete deposits, where leach residence time of 96 hours is often required.

Figure 10‑3: Leach behaviour across all Domain composites.

 

10.3     Solid Liquid Separation and Dewatering

The upgrade of carnotite by screening naturally results in concentration of clay minerals. A program of rheological characterisation, including thickener and filtration modelling was undertaken at ANSTO Minerals by Rheological Consulting Services. Vendor test work was undertaken on pressure filtration by Aqseptance in 2022, confirming DFS assumptions.

10.4     Ion Exchange

Uranium was recovered from clarified pregnant leach liquor by Ion Exchange at ANSTO Minerals. Ion exchange was undertaken using a fixed bed in lead-lag configuration with a Strong Base Anionic (SBA) Resin. For a nominal 98 % extraction of uranium from the PLS (670 mg/L U₃O₈), very close to the maximum loading can be achieved with resin inventories of ~0.15 m³ resin per m³/h of PLS.

10.5     Uranium Precipitation and Purification

Uranyl peroxide precipitation sighter tests were performed using a portion of the sulphuric acid digest solution, by the addition of hydrogen peroxide at controlled pH. Samples of the feed and final liquors were analysed by ICP-OES and ICP-MS. The UO₄ was washed, dried, digested in nitric acid and analysed by ICP-OES and ICP-MS. A vanadium removal test was performed by adjusting the SDU digest liquor to approximately pH 2 at 50°C, prior to UO₄ precipitation at pH 3-4.

10.6     Uranium Oxide Concentrate Product

Uranium Oxide Concentrate (UOC) in the form of UO₄ was produced by ANSTO Minerals from concentrate samples generated in the Mintek beneficiation pilot plant. The results shown in Table 10‑1 demonstrate that the product is within ASTM standard specification limits without rejection.

	UO4 wt% U Basis	Limit Without Penalty	Limit Without Rejection
As	<0.001	0.05	0.10
B	<0.07	0.01	0.10
Ca	<0.001	0.05	1.00
K	0.06	0.20	2.00
Mg	<0.001	0.02	0.50
Mo	<0.001	0.10	0.30
Na	0.07	0.50	7.50
P	<0.07	0.10	0.70
S	0.13	1.00	4.00
Si	<0.04	0.23	1.17
Ti	<0.001	0.01	0.05
V	0.02	0.06	0.30
Zr	0.01	0.01	0.10
Cl	0.02	0.05	0.10
F	<0.004	0.01	0.10

Table 10‑1: Tiris UO₄ precipitate impurity concentrations with reference to ASTM standards limit without penalty or rejection.

The results generated from bulk metallurgical test work program at ANSTO Minerals on concentrate samples from beneficiation pilot program (see JORC Table 1 below and ASX Release: 23rd June 2022)

 

 

11        Process Plant

The uranium is hosted with ultra-fine grained carnotite (K₂(UO₂)₂(VO₄)₂.3H₂O) that is loosely attached to barren gangue particles. This means uranium-bearing carnotite can be readily separated from barren particles, allowing highly efficient upgrade of uranium concentration by simple scrubbing and screening. This greatly reduces the mass of material for leaching, reducing footprint and throughput for the hydrometallurgical plant.

The processing facility consists of three main sections. These are separated by surge tanks and include:

·    Beneficiation circuit

·    Uranium extraction circuit (Alkaline leach - solid liquid separation - Ion exchange)

·    Uranium purification and precipitation circuit.

There are several process configurations used for recovery and extraction of uranium, predominantly driven by the type of uranium mineralisation. Leaching of uranium can be undertaken in either acid or alkaline conditions. The selection of the leaching system is driven by the ore composition and whether acid or alkaline consuming minerals are dominant. In the case of the Tiris calcrete mineralisation, acid consuming minerals (e.g. calcite and strontianite) are prevalent and preferentially concentrate with the uranium bearing carnotite. Therefore, the Tiris mineralisation is well suited to uranium recovery by alkaline leaching, using the sodium carbonate/ sodium bicarbonate system. The leach is undertaken at a temperature of 90°C with a residence time of 12 hours.

The main commercial process options for solution recovery after leaching are counter current decantation (CCD) using high-rate thickeners, or filtration. The elevated clay concentration in Tiris leach product means that settling rates are low, and the wash efficiencies for a CCD circuit would be similarly low. This would result in increases in the water balance and high losses of contained reagents. Alternatively, for filtration, while clays lead to slower filtration rates, the efficiency of solution recovery is greater. This leads to more efficient reagent recovery, and higher uranium concentration in feed to recovery circuit. To reduce filtration time the Tiris process utilises a filter-repulp-filter configuration, where washing of the slurry is undertaken in a repulp tank, rather than inside the plate and frame filter.

For alkaline systems the main process options available for recovery of uranium are ion exchange (IX), Resin in Pulp (RIP), or Direct Precipitation. For the Tiris process, ion exchange was selected. For efficient application of Direct Precipitation higher concentrations of uranium in leach solution would be required, to minimise downstream reagent requirements. Similarly, the elevated clay concentration may cause 'blinding' of resin in an RIP system, reducing recovery efficiency.

After ion exchange the resin loaded with uranyl carbonate is eluted using sodium bicarbonate. The eluted uranium stream is then further concentrated by nano-filtration, and sodium bicarbonate recovered for recycle back to the leach circuit. Uranium is then precipitated with sodium hydroxide as sodium diuranate (SDU). The SDU precipitate is filtered and dissolved in sulphuric acid as uranyl sulphate, ready for final precipitation.

Uranium is precipitated with hydrogen peroxide to form the final uranyl peroxide (UO₃) product. UO₄ will then be dried or calcined to form the final Yellowcake product. Yellowcake is a term used to cover all Uranium Oxide Concentrates (UOC), which may include UO₄, UO₃, UO2 or U₃O₈.

The final UOC product will be packed in secure 205L IP-1 open head steel drums and strapped within a 6m container for transport by road to the Port of Nouakchott.

Figure 11‑1 summarises the Block Flow Diagram for the process and Figure 11‑2 shows the proposed plant layout.

Figure 11‑1: Process block flow diagram

 

 

Figure 11‑2: Processing Plant Layout

 

11.1     Processing Trains

The 2021 DFS provided a base case for design of 1 modular processing train. A modular design was selected to allow simple addition of additional processing trains to facilitate expanded production. On this basis the Enhanced Feasibility Study has assessed expansion options through incremental addition of modular units.

The design capacity of modular process trains is:

·    Beneficiation circuit: 1.25Mtpa Run of Mine (ROM) ore.

·    Leaching, IX and precipitation circuit: 230,000tpa Leach feed.

·    Precipitation and Packaging circuit: 3.5Mlb per year UOC.

 

11.2     Modular Beneficiation circuit

The Tiris Eastern resources are spread over 64 km east-west and 36 km north-south, so the transport of ore is a significant consideration. Refer to Figure 11‑3 for spread of Tiris resources.

The Tiris mineralisation allows for rejection of 85-90% of ore mass as barren rejects, through a simple beneficiation process. To optimise the material transport, a modular transportable beneficiation circuit located close to the resources was incorporated. The trucks have a transport distance of around 1-2 km to the beneficiation stage, and slurried product is pumped to the processing plant. Refer to Figure 6 for process plant location at Lazare centroid.

The modular beneficiation circuits and the hydrometallurgical process plant are in separate locations connected by pipelines, used to transfer slurry, liquid recycling, and raw water.

The ramp up mine schedule focuses on mining of Lazare South resources over the first 2 years with a single modular beneficiation circuit. In stable operation from year 3, mining hubs will be established at the Lazare, Sadi and Hippolyte Resources, each with a modular beneficiation circuit. The beneficiation circuit has been designed to be transportable. Given that this will stop all production until all the plant systems and utilities are re-connected and re-commissioned, a highly planned shutdown will be required. An allowance of 4 weeks to shift the beneficiation circuit each time has been made in the mine schedule.

The modular and transportable front end beneficiation circuit comprises: -

·    ROM ore Feeder-Breaker unit

·    Rotary wet scrubber 2.4 m diameter x 4.8 m long.

·    3 sets of 2 screens with screen apertures of 2mm, 300 micron and 150 microns.

·    Waste conveyor and radial stacker for the 85% rejects.

·    Agitated surge tank for storing slurry

·    Slurry pumps to pump slurry some 6 km to Process plant

Figure 11‑3: Resource distances to Lazare processing plant

 

Figure 11‑4: Optimized (Opex/Capex) site location for Lazare Resources

 

11.3     Modular processing circuit

Connecting the Beneficiation front end and the permanent process plant, there are 3 surface run HDPE pipelines some 6 km long as follows: -

·    The 225 DN, PN25 PE 100 fines slurry line transferring pumped slurry to the process plant,

·    The 200 DN, PN 25 PE 100 liquor recycle line returning filtrate from the process plant to the beneficiation front end,

·    The 32 DN, PN16 PE 100 raw water supply line providing raw water to the beneficiation front end.

These will be fully welded into section lengths able to be safely dragged without damage, during the relocation stages. Flanges would connect the section lengths.

The Process plant major equipment shown in Figure 11.5 comprises: -

·    A hi-rate carbon steel pre-leach thickener, ten metres diameter with three metre walls,

·    Four agitated surge tanks, providing 24 hours downtime capacity for the downstream process plant,

·    A 650m2 filter press feeding a cake transfer conveyor,

·    Six agitated leach tanks 6.1 m diameter, 6.4 m high,

·    A diesel steam boiler package and two associated heat exchangers, to heat the slurry to 90 degrees C,

·    Three 26 m long plate and frame filters filtering the barren liquor from IX, and filtrate from product dewatering,

·    IX feed tank and three IX columns,

·    SDU Precipitation circuit, including thickener, decanter centrifuge and tanks.

 

Figure 11‑5: Isometric plan of leach, ion exchange and precipitation circuits

 

11.4     Modular precipitation and packaging circuit

A modular, containerised precipitation and product packaging circuit shown in Figure 11.6 has a  design capacity to produce up to 3.5Mlb per year UOC will be used, including:

·    Product Precipitation plant including fluid bed crystalliser, dewatering centrifuge, 150 kW rotary kiln, vent scrubber, and drum packaging plant.

The Modular Dewatering, Drying/Calcining and Drum Packing Plant will be pre-assembled modules. They will be located within the main plant perimeter in a secure building, with restricted and controlled personnel access.

The dewatering, drying, off-gas modules, dust collector and yellowcake buffer hopper will be in an enclosed and sealed area of the Drum and Packaging (D&P) building, to prevent any fugitive dust from escaping from the process plant area. The Drum Packing Module will be on the clean side of the D&P building.

Figure 11‑6: Isometric plan of UOC drying and drum packaging plant

 

11.5     Ramp up Phase

The mine schedule has been developed to allow for a ramp up phase of two years. This will provide Aura with the opportunity to stabilise operations, logistics and fully train the workforce.

The ramp up phase, with mining rate of 1.25Mtpa ROM material, will include circuits at design capacity summarised in Table 11‑1

Modular Circuit	Number circuits	Design Capacity
Beneficiation	1	1.25 Mtpa
Leaching, IX, Precipitation	1	0.23 Mtpa
Product precipitation and packaging	1	3.5 Mlbs pa UOC

Table 11‑1: Circuit configuration for ramp up phase.

 

 

11.6     Operations

Through the ramp-up phase procurement and construction will be undertaken for additional modular circuits to achieve full operational capacity. The incremental addition of modular circuits provides Aura with the capacity to tailor expansion in a capital efficient manner, with minimal operational risk.

The operation will target a mining rate of 4.18Mtpa ROM material and will include modular circuits with design capacity summarised in Table 11‑2.

Modular Circuit	Number circuits	Design Capacity
Beneficiation	4	1.25 Mtpa
Leaching, IX, Precipitation	2	0.23 Mtpa
Product precipitation and packaging	1	3.5 Mlbs pa UOC

Table 11‑2: Circuit configuration for operations phase.

 

 

Figure 11‑7: Flow diagram of process circuit configuration through start up and operations phases.

 

Test work has demonstrated that beneficiation at a screen cut size of 75µm is readily achievable. It has been assumed that in stable operations these screening conditions will be used, resulting in higher leach feed grade and more efficient use of modular leach circuit capacity.

The profile of leach feed material can be seen in Figure 11‑8.

 

Figure 11‑8: Beneficiation ore (leach feed) and grade profile for LOM

 

The U₃O₈ production profile across the Life of Mine (LOM) can be seen in Figure 11‑9. This shows an average U₃O₈ production rate of 2.0Mlb per year through the first 10 years of the operations phase.  Peak UOC production of 2.4Mlb pa U₃O₈ will be achieved in year 4.

 

Figure 11‑9: U₃O₈ production profile with recovery for LOM

 

11.7     Tailings

The permanent process plant produces a 300,000m3/year tailings stream from the leach pressure filtration module at 25% moisture content. The leach plant tailings would be stockpiled on a slab by a belt conveyor and loaded by a front-end loader into mining trucks. For approximately the first 6 months, the tailings would be transported to tailings dam some 1,100m northeast of the plant. The tailings dam would hold 75,000m3 of tailings, with dimensions 250m by 180m by 2m deep. When adequate voids are available in the mined-out areas, the dewatered tailings would be trucked directly to the mined-out areas for in-pit disposal, at the base of the pits. The tailings would then be covered by barren reject material, mine waste and overburden.

It has been assumed that no lined geotechnical membrane will be required underlying the tailings dam. Aura will have to confirm from testing the likely concentration of radiation levels in leach plant residue, and whether any groundwater issues will be caused. The required waste and overburden coverage above the tailings requires confirmation.

At the front-end beneficiation plant, there is a barren rejects stream produced of coarser material (2,100,000m3/year) discharged from the 3-stage screening unit. This reject material will be predominantly between 2mm and 75µm in size and be initially used to build berms on the windward side of the pits to reduce dust levels. Once sufficient voids are available in the mined-out pits, these rejects would be back filled into the mined-out areas, and subsequently covered with mine waste and overburden. Having the front-end plant within 1km of the open cut pit reduces trucking to reasonable levels.

 

11.8     Water Supply

In the ramp up phase the 1.25 Mtpa process operation requires between 0.5 and 0.6 Gl of water per year, supplied to the plant. Of this, 150 litres/person/day is required for personnel use, and 0.17 Gl of raw water for dedusting roads and ongoing roadworks. Only some 40,000 m3, (or 7%) needs to be converted by a water treatment plant to demineralised or potable quality, as the process can utilise water with a moderate degree of salinity.

Of 4 regional water sourcing options initially identified by hydrological consultants, Aura's water search and development activities have focussed on the closest source, the Oued El Foule Depression, an extensive drainage system, the central axis of which is less than 20 km from the Tiris plant site.

Aura identified a number of major structures likely to host water and carried out ground geophysics (resistivity and EM) over 24 targets within 50 km of the proposed plant. 15 of the most promising targets were selected for drilling. To date 6 of these targets have been drill tested, three of which yielded significant water flows. The best of these, Target C22, was followed up with detailed ground geophysics for optimum siting of drill holes. C22 was tested by 8 water bores and 5 monitoring holes, and 72-hour pump testing was carried out on 7 of the bores.

The C22 aquifer is relatively shallow with standing water level starting at 28m depth and no water deeper than 61m in drilling to date. While C22 contains sufficient water to supply the operation for many years at 0.6 GL/yr, modelling by Groundwater Exploration Services Pty Ltd in Australia, has suggested that due to porosity and permeability characteristics of the aquifer a pumping rate greater than 0.25 GL per year may not be able to be sustained.

The C22 aquifer remains open at its southern end where the best water flows were encountered.  A program of geophysics completed in this area has indicated good prospects for extending the aquifer to the south, and a drilling program to test this has been prepared.

Additionally, the strike rate in water drilling to date and the number of targets yet to be tested indicate a strong likelihood that drilling will locate additional water supply for the relatively low water requirement of the Tiris Project. Two producing water bores (shown in figure 11.10) were drilled by the Mauritanian Government to supply informal mining activity and demonstrate the presence of reliable water supply within 70 km of planned operations.

 

Figure 11‑10 - Water drill hole locations in relation to project area

 

Figure 11‑11 - C22 aquifer

 

Figure 11‑10 shows the location of the six water bores drilled to date, and the C22 aquifer in relation to mining leases and planned operations. The two producing water bores shown in green were drilled by the Mauritanian Government to supply informal mining activity and show the presence of reliable water supply. Figure 11‑11 shows drilling within the C22 aquifer, along with measured flow rates.

 

Small 24 kW dedicated diesel generators will be used at each borehole to power the 11 kW submersible lift pumps, and the 3kW transfer pumps. Similarly, a 48 kW diesel generator is required at the main pumping station, to power the duty and standby 37 kW pumps. The local fuel tanks will have a two week capacity and be supplied by an Aura fuel truck or trailer from the main process plant diesel storage. Telemetry will be installed to provide the control linkage and hourly reporting, back to the main process plant.

The twelve-hour capacity raw water storage tank at the process plant, will supply water for firefighting, dust suppression and to the Reverse Osmosis (RO) water treatment plant.

The containerized RO water treatment plant will produce both potable and demineralized water, with storage for 48 hours potable water and 4h demineralized water. Water will then be reticulated from these tanks to accommodation, administration, and laboratory buildings as well as to the process plant, and to the camp via a 3 km pipeline. Potable water requirements for the transportable front end and mining offices will be trucked down in a suitable water tanker, to smaller portable tanks there.

 

 

 

12        Infrastructure

The infrastructure component of the Tiris Project includes all supporting facilities located outside the mining area. Infrastructure includes the engineering design, procurement and management for the following site infrastructure works:

·    Internal roads within the process site, and minor roadworks on the 680km site access road from Zouérat.

·    Bulk earthworks

·    Accommodation camp installation, reticulated services, waste disposal, water treatment and associated infrastructure.

·    Transportable buildings including offices, change rooms, crib rooms and ablutions.

·    Communications systems

·    Steel framed buildings including workshops, warehouse, and uranium packaging building.

·    Power reticulation across the project site.

·    Site security. 

·    Process plant security.

·    Remote water borefield and pipeline.

 

12.1     Site Works

The process plant area includes a heavy vehicle workshop, which will carry out maintenance on all the mining fleet. All the designated road areas within the process plant area, and the process plant equipment area, will require some soil compaction to avoid settlement. Key process equipment/traffic areas will be prepared by stripping the topsoil, proof rolling the area and installing a crushed compacted granite sub-base. Earthworks will thus be limited to the minimum required only. No earthworks are planned for the camp 3km northeast of the process plant, due to the low building weights involved.

 

12.2     Access Road

Figure 12.1 indicates the route proposed utilising trucking on the existing 767 km N1 sealed highway from Nouakchott port to Zouérat. From Zouérat, there is initially 15 km of sealed road, then a 665 km unsealed desert track to Tiris.

Some limited road works will be required on the 665 km unsealed section prior to construction commencing, to ensure all trucks (2WD & 4WD) can reliably travel from Zouérat to the Tiris site in two days. The route will be marked clearly, and soft sand sections replaced with crushed compacted rock fill. A permanent road maintenance crew will then be required during construction and ongoing operations to keep the road in satisfactory condition.

Figure 12‑1: Proposed site access route from Nouakchott via Zouérat

 

12.3     Accommodation Camp

The camp will consist of accommodation for 200 personnel in total, including an allowance of visitors. Security, kitchen and dining facilities, a large recreation room, a prayer room and storage facilities will be provided. Camp accommodation and support buildings will be located some 3km north-east of the plant site, to reduce the effects of windblown dust and noise from the operations.

Figure 12‑2: General view of accommodation camp

 

12.4     Communication Systems

Aura will install a fully managed VSAT solution, coupled with Wireless and Wi-fi extensions. Satellite telecommunications systems are well proven, given that numerous other remote mining companies in Africa are using similar systems.

A guaranteed pool of 10 Mbps dedicated bandwidth will be provided. It will be dynamically allocated as required between the VSATs, with input by Aura. Wi-fi connectivity then extends coverage within the Aura transportable front-end and mine buildings, process plant and camp.

 

12.5     Electrical Power Supply

The electrical power supply for the Tiris plant comprises supply of power to four separate locations as follows:

·    The transportable front-end plant comprising beneficiation, screening, and slurry pumping.

·    The permanently located process plant comprising leaching, ion exchange, precipitation, and carbonation, SDU purification, UO4 precipitation and packing, workshops and administration facilities.

·    The permanently located construction/operations camp 3.3 km NE of the process plant, supporting 200 bed accommodation with kitchen/dining room, recreation hall, prayer room and camp management offices.

·    The remote water borefields and water pumping station some 31 km southwest of the process plant.

The following table summarizes the total power peak demand per area and the related power generation required (Table 12‑1)

Area	Peak Demand (kW)	DG installed power (kW)	Solar installed power (kW)
Front-end	1,829	5 x 400	-
Permanent Plant	3,564	4 x 1,200	2,160
Camp	650	From plant	From plant
Remote water supply	225	3 x 48 4 x 48	-
Total	6,268	7,136	2,160

Table 12‑1: Electrical load requirements for the Tiris Project in full operation.

 

The camp is powered through a 3km long overhead 11 kV powerline from the Process power plant, with 415V/11Kv transformers at either end.

The Transportable Front-end plant is powered by diesel generators, which is a more economical solution rather than a MV/HV powerline from the permanent process plant. Relocating the front-end four times in the first ten years of operation will be easier with transportable generators.

The permanent plant site and camp have an estimated peak demand of 3,370 kW, requiring four off 1,500 kVA diesel-powered generators. Two will operate most of the time, with one on standby and one for redundancy.

A 2,160-kW solar power plant will provide most of the permanent plant electricity during daylight, with solar supplying 30% of the total energy consumed per year.

 

12.6     Airstrip

Charter flights to site for medical evacuations and essential executive travel will initially use the existing Shield Mining airfield, located 152 km from the site. Re-licencing is required for this 1,100m long by 39m wide airstrip.

After a few years of operation, a daylight hours airstrip is expected to be built on the project site, some 2km from the Tiris process plant.

Figure 12‑3: Existing Shield Mining airfield

 

12.7     Zouérat Offices, Administration and Guest House

Aura Energy will need to set up an administration office based in the key location of Zouérat. Zouérat will be the key source of much site labour, and initial inductions and training required would be carried out there. During Construction and Operations, workers would be bussed the 680 km to site from Zouérat by Aura's bus fleet.

A local guest house with dining facilities will also be required for the frequent stopover periods of expatriate specialists or management flying into Zouérat from Nouakchott and travelling on to site.

 

13   Environmental and Permitting

A comprehensive Environmental and Social Impact Assessment (ESIA) was completed in 2017 by Earth Systems, an internationally recognised consulting group with extensive experience in mining and uranium extraction.

The ESIA pays close attention to issues of radiation exposure and security of the uranium 'yellowcake' product. Throughout the ESIA and the associated project design and management measures, best practice guidelines from the International Atomic Energy Agency (IAEA) and the International Commission on Radiological Protection (ICRP) have been used, complementing the applicable Mauritanian regulations and guidelines.

ESIA was fully approved by the Mauritanian Government on 5th October 2017

13.1     Physical Setting

13.2     Climate and Meteorology

The project is in the hyper-arid zone of northern Mauritania receiving only very rare rainfall. Annual average rainfall rarely exceeds 20 mm around the Eastern resources and 50 mm around the Western resource.

The region is subject to Harmattan winds, a north-easterly trade wind that occurs during dry conditions and can result in extensive and dense clouds of dust that can form dust or sandstorms.

13.3     Naturally Occurring Radioactive Material (NORM)

Uranium in the environment is a form of Naturally Occurring Radioactive Material (NORM). The uranium mineralisation targeted by the Tiris Uranium Project is a near-surface accumulation of carnotite (potassium uranium vanadate) that has formed by cyclical near-surface weathering, dissolution, evaporation and reprecipitation.

The annual NORM radiation dose in the resource areas is predominantly in the range 0.02-1.7 mSv/y, with fewer than 1% of readings above this value (up to 23 mSv/y). The worldwide average annual radiation dose from natural sources is 2.4 mSv/y but due to elevated NORM sources, some areas can be as high as 6-12 mSv/y.

13.4     Air Quality

Dust is the main determinant of air quality in the project region. Natural wind-blown dust levels are typically high and likely to exceed international inhalable particulate health criteria on a regular basis.

13.5     Social Setting

The project is in a very sparsely populated region of the Sahara Desert, in a designated military Prohibited Zone. This Zone is enforced due to smuggling activity across adjoining borders.

The nearest permanent settlements are Bir Moghrein (pop c. 3000), 460 km west of the Eastern Tiris Resource Area), and provincial capital Zouérat (pop c. 45,000), 620 km west southwest. Other populations in the region include a small military base at Cheggat, 105 km from the Eastern Tiris resources, a small military outpost at Ain Ben Tili, 15 km north of the Western Tiris Resource Area, and a small settlement located across the border in Western Sahara within 20 km of the Western Tiris Resource Area.

No nomadic groups were identified in the broader region surrounding the Eastern Tiris Resource Area, and the area is not in the normal range of nomadic families.

Artisanal gold miners make temporary settlements in the region, and there is currently such a settlement 55 km southeast of the project at Gleib Ndour.

13.6     Land and Water Use

There is no permanent land use in the vicinity of the project areas.

13.7     Archaeology and Cultural Heritage

A survey of the project areas and surrounds in January 2017 identified 29 archaeological sites (principally burial sites) in the vicinity of the project areas (12 at the Eastern Tiris Resource Area and 17 at the Western Tiris Resource Area). Five additional sites of cultural heritage significance are in the broader area surrounding the project.

 

 

13.8     Risk Assessment

13.8.1   Radiation Impacts and Measurement

Careful management will be applied when extracting and processing the uranium mineralisation to prevent or minimise potential radiation exposure for workers, the public and the surrounding environment. The project will produce on site a uranium ore concentrates (UOC) or 'yellowcake', in a benign oxide form. UOC is not toxic, has low radioactivity and is safe to transport. UOC is not fissile, it does not undergo any nuclear reaction and has no use or value without technological enrichment. Enrichment is only conducted at a small number of highly regulated enrichment facilities around the world. The activities at the Tiris Uranium Project deal only with naturally occurring materials, and do not create any 'new' sources of radiation.

13.8.2   Terrestrial Fauna

The estimated exposure of terrestrial fauna to radiation associated with project activities is 0.045 mSv/d (15.88 mSv/y), which is significantly below the US Department of Energy guideline (DOE-STD-1153-2002) levels (20 times lower). The risk of radiation impacts on fauna is therefore expected to be negligible.

13.8.3   Terrestrial Flora

The Eastern Tiris Resource Area is devoid of vegetation and the Western Tiris Resource Area is only sparsely vegetated with grasses in limited areas. The estimated exposure of terrestrial flora to radiation associated with project activities is 0.044 mSv/day (15.70 mSv/y). The total estimated radiation dose is significantly below the guideline levels (200 times lower) indicating that the risk of radiation impacts on flora is expected to be negligible.

13.8.4   Aquatic Ecology

Fugitive radioactive dust could accumulate in surface waters following rare rainfall which could result in the risk of radiation exposure to aquatic biota. However, the residual impact is expected to be negligible.

13.8.5   Land Use

With no permanent settlements or land use in the vicinity of the project, impacts on existing land use are expected to be negligible throughout construction, operations, de-commissioning, and post-closure.

13.8.6   Terrestrial Biodiversity

There are no international, national, or regional protected areas or reserves in proximity to the project areas.

The small amount of habitat loss associated with the siting of project infrastructure is not likely to be significant for species conservation in the region. No species are expected to be lost due to the development of the project or have a significant proportion of their range affected.

13.8.7   Hydrology

Due to the rarity of rainfall and absence of surface water, the overall expected impact of the project on hydrology is expected to be negligible. However, the risk of flooding during rare rainfall needs to be considered in the siting and design of project components, to protect project personnel and infrastructure.

In the production bore area, the expected impact of the project on local hydrogeology is expected to be low due to local temporary groundwater drawdown, and the absence of beneficial users.

During the Operations Phase, the expected impact of the project on water quality is expected to be low and localised. The principal residual risks are:

·    the potential for water contamination during flood inundation should such inundation exceed design flood controls

·    and the low potential for downstream accumulation of wind-blown dust that escapes project dust management measures.

Post-closure, the site will be returned to the pre-development landform and soil/overburden cover, including the removal of any identified surface contamination. The post-closure impact of the project on water quality is expected to be negligible.

The naturally high ambient dust levels of the region will be one of the principal concerns for workers' health. Ambient air quality in the region has the potential to exceed IFC/WHO air quality guidelines during dust storms and Harmattan dust haze events.

The primary potential air quality impact associated with project activities is the potential for fugitive dust emissions from mining and processing. Dust modelling indicates that dust emissions are expected to be localised within the vicinity of operations. There are no permanent settlements in the vicinity of the project areas or on the route, and no significant wildlife or vegetation. Therefore, dust generation from mining, processing and transport activities is not expected to result in any significant impact beyond the worker community.

13.8.8   Archaeology and Cultural Heritage

No World Heritage Sites or otherwise internationally recognised archaeological or cultural heritage sites are located close to the project.

No archaeological sites were identified in the current resource zones, however, eight sites were identified within 250 m of a resource zone and will require management to avoid potential indirect impacts. Allowance has been made for fencing or relocation of any affected archaeological sites.

No cultural heritage sites were identified in proximity to the project areas and no cultural heritage impacts are expected.

13.8.9   Cumulative Impacts

The project lies in a remote, underdeveloped, and unpopulated area of the Sahara Desert and cumulative impacts associated with the project are therefore expected to be minimal.

The project is expected to help progress the socio-economic development of the region through procurement of goods and services and continue the development of Tiris Zemmour as an important economic area for Mauritania.

13.8.10 Other Impacts

Other potential impacts likely to be associated with the development of the Tiris Project are:

·    Traffic and transport: The principal transportation route from Zouérat to Tiris is unpopulated, lightly trafficked by other road users, has few nearby settlements, and is subject to controlled access under military authority. Some roadworks will be required on the 665km desert track to ensure 2WD construction traffic can make this trip in 2 days in daylight. Implementation of the management and mitigation measures outlined will ensure that potential impacts are minimised.

·    Community health and safety: The project is expected to improve local health facilities and services directly and indirectly in the Tiris Zemmour region through the implementation of a community development program, and the economic development and employment opportunities created. Potential community health risks and potential health impacts are expected to be very low or non-existent for the Tiris Project due to the remoteness of the project site.

 

14        Project Implementation

The approach proposed for the engineering, procurement, logistics, construction and commissioning of the Tiris Uranium plant and infrastructure is summarised below. The project will be run by the following parties, coordinating with each other:

Owner's team: dedicated team from Aura.

Main engineering contractor: Australian engineering company with African and modular knowledge and experience, providing the Engineering Procurement or EP components.

Technology suppliers: engineering companies for the two main parts of the process plant, where specific knowledge and experience about uranium processing is required. These two suppliers are virtually turnkey designers, but with site commissioning only.

Vendors: companies from around the world that will supply the different equipment and material.

Site contractors: companies mainly from Mauritania or with experience in the country, that will perform the installation works, providing services required in country and on site.

Logistics contractor: responsible for all construction equipment pick up, delivery to port, shipping, customs clearance and transport to Aura's site warehouse at Tiris.

The strategy is to contract the main engineering contractor to engineer and procure. This involves managing procurement of supply packages, and setting up the site installation contracts for and on behalf of Aura. The owner's team is then responsible for construction management, including the site contract administration with site installation contractors.

As some of the detailed process technology will be provided by others, the main engineering contractor will act as an "Integrator" for various aspects of the project. Where equipment is supplied by others, this involves integrating the equipment interfaces with the balance of the plant, including foundations, steelwork, piping and electrics. The main engineering contractor also ensures that all services required by the equipment are provided, e.g. power, water, compressed air.

At practical completion the main engineering contractor supplies all drawings, documentation and Operating and Maintenance manuals required to run the plant.

 

15   Project Schedule

The Tiris Project schedule is expected to have the following time scale to undertake site works and commission the first modular process train:-

·    Commence FEED Study for initial modular circuits in January 2023 (commenced).

·    Final Investment Decision in Q4 CY 2023,

·    Long lead item orders placed in October 2023.

·    Detailed engineering design commencing immediately taking 9.5 months and being largely complete by mid-month August 2024.

·    Site and camp establishment to commence in Q4 CY 2023

·    Allowing the main construction contracting to commence in January 2024 and be completed in 12.5 months in mid-month 22.

·    Commissioning to commence in Q4 CY 2024, with the first UOC production in December CY 2024.

·    Operations start-up after completion of commissioning, in Q2 CY 2025, with first UOC sales.

 

This gives an overall start-up project duration of 27 months from kick-off to commercial sales as illustrated in Figure 15.1 below.

Ramp-up of operations will begin in H2 CY 2025 with long lead item procurement and detailed engineering for an additional 3 modular beneficiation circuits and 1 leach circuit:-

·    Long lead item procurement from July 2024.

·    Detailed engineering, contracts and procurements commencing December 2024, to be completed in 11 months, by Q4 CY 2026.

·    Construction for expansion modular circuit to commence Q2 CY 2026, taking 9 months for completion by the end of December 2026.

·    Commissioning to commence September 2026 for completion by February 2027.

This gives an overall ramp-up project duration estimate of 18 months from placement of long lead item orders to full stable operation.  The efficiency is gained through the replication of design components within modular circuits and minimal requirements for additional infrastructure.