Clean TeQ Water Ltd · ASX:CNQ

Clean TeQ Water — Technical Presentation (December 2023)

24 slides from Clean TeQ Water's technical presentation, December 2023

  1. Slide 1: Continuous Direct Lithium Extraction cDLE®

    Continuous Direct Lithium Extraction cDLE® Peter Voigt, CTO G2L December 2023 Direct Lithium Extraction 2023

  2. Slide 2: Brought to you by

    Brought to you by World’s leading Direct Lithium Extraction technology with proven pathway to full-scale commercial plant Value generation Partnering in a company that provides access Go2Lithium Inc and LithiumBank to one of the largest lithium assets in Northern Resources Corp Partnering to Develop

  3. Slide 3: Our Footprint

    Our Footprint Companies Projects Clean TeQ Europe Project: Ordos Netherlands Nitrate removal, mine water Commercial Office & Lab treatment Clean TeQ China Commercial Office & Lab Project: Oman Antimony processing water treatment Computational Geosciences Vancouver Commercial Office Project: DRC Uran

  4. Slide 4: Why DLE?

    Why DLE? Compared to hard rock mining and salar evaporation SIMPLE PROCESS BETTER LITHIUM FASTER PRODUCTION LESS LAND AREA LESS WATER INPUT LESS GREENHOUSE GAS LESS TIME TO RECOVERY RATES (GHG) EMISSIONS PRODUCTION December 2023 Direct Lithium Extraction 2023 4

  5. Slide 5: DLE Challenges

    DLE Challenges LITHIUM LOADING CAPACITY ELEMENTAL SELECTIVITY SPECIALTY REAGENTS WATER LOW LOADING REDUCES POOR SELECTIVITY INCREASES INCREASES COST AND PROCESS HIGH WATER USE INCREASES ECONOMIC VIABILITY LOADS TO THE REFINERY COMPLEXITY COST ENERGY AND CSG IMPACT OUR CONTINUOUS DLE (cDLE®) TECHNOLO

  6. Slide 6: LithiumBank cDLE®

    LithiumBank cDLE® Li Ion Sieve Mineral sorbent Options: Important Sorbent Parameters: • Adsorption • Loading capacity • Ion Exchange (Li Ion Sieve) • Selectivity • Solvent Extraction • Sorption kinetics • Membranes • Desorption chemistry Resin sorbent • Desorption kinetics https://nextinvestors.com/

  7. Slide 7: Sorbent characteristics

    Sorbent characteristics R-H+ (s) + Li+ (l) → R-Li+ (s) + H+ (l) R- ion exchange sorbent A A 70ppm B 70ppm Sorbent B Sorbent Loading Loading mg Li/g mg Li/g 1ppm 3ppm 1 10 50 100 1 10 50 100 Concentration in Solution mg Li/L Concentration in Solution mg Li/L A is better than B A is better than B Dec

  8. Slide 8: Sorbent characteristics

    Sorbent characteristics R-H+ (s) + Li+ (l) → R-Li+ (s) + H+ (l) R- ion exchange sorbent pH v’s Loading Capacity 7 6 Stage 2 5 Loading “tail” Sorbent Sorbent 4 meq/g Loading Loading mg Li/g mg Li/g Stage 1 3 2 Stage 1 Stage 2 1 Desorption “tail” 0 Sorbent Loading Time (hr) Sorbent Desorption Time (h

  9. Slide 9: Sorbent specifications

    Sorbent specifications Highest loading capacity Good Reasonable selectivity for cost Li over Na, Ca, Mg Fast initial Mechanical sorption stability kinetics Reasonable Chemical kinetics to stability maximum loading December 2023 Direct Lithium Extraction 2023 9

  10. Slide 10: cDLE® selection for LithiumBank

    cDLE® selection for LithiumBank • Sorbent plus cDLE® • Process • Ion Exchange or Sorbent • Adsorbent • Fixed Bed • Carrousel Process • Continuous counter-current sorption, & • desorption • Static Bed Column • Continuous Moving Packed Bed, or cDLE® Contactor • Continuous Fluid Bed, or • Continuous St

  11. Slide 11: Continuous Ion Exchange Process

    Continuous Ion Exchange Process https://youtu.be/2hgPLwmL2Ww December 2023 Direct Lithium Extraction 2023 11

  12. Slide 12: cDLE® Moving Packed Bed

    cDLE® Moving Packed Bed H+ loaded Sorbent Li+ loaded Sorbent Barren brine Sorption Wash Desorb Wash Weak Lithium Wash Feed brine to eluate recycle brine recycle to refinery to feed Sorbent Flow Desorption Wash water Wash water solution

  13. Slide 13: cDLE® CSTR

    cDLE® CSTR Li+ Sorbent H+ Sorbent Li+ Sorbent Li+ Sorbent H+ Sorbent Sorption Sorption Sorption Sorption Wash Desorb Wash Barren Weak Lithium Wash Feed brine brine eluate recycle brine Sorbent Flow to feed recycle to refinery Desorption Wash water Wash water solution

  14. Slide 14: LithiumBank cDLE® Chemistry

    LithiumBank cDLE® Chemistry cDLE® Feed cDLE® Eluate 60,000 4,000 56,719 3,500 3,401 50,000 3,000 40,000 2,500 mg/L mg/L 30,000 2,000 22,390 1,500 20,000 1,000 10,000 416 463 500 4,216 274 2,630 138 114 931 25 21 8 10 3 70 8 0 0 - - B Ba Ca Fe K Li Mg Na Si Sr B Ba Ca Fe K Li Mg Na Si Sr December 202

  15. Slide 15: cDLE® Benefits

    cDLE® Benefits cDLE® transforms the economics of low-grade lithium resources 1 2 3 4 5 More revenue Lower opex Lower energy Better environmental Lower opex credentials Lithium Recovery Chemical Inputs Lithium Tenor Refinery Size Water Use cDLE® DLE DLE DLE cDLE® 92-98% 100% 100% 100% 3-10 1,500/t g/

  16. Slide 16: cDLE® improves npv for lithium extraction

    cDLE® improves npv for lithium extraction December 2023 Direct Lithium Extraction 2023 16

  17. Slide 17: Next steps

    Next steps Aug 2023 Nov 2023 Feb 2024 Feb – Dec 2024 2025 Technical Licence Demonstration Plant Pilot Plant operational in Operate Pilot PFS Agreement ships to Canada Calgary PFS Inputs December 2023 Direct Lithium Extraction 2023 17

  18. Slide 18: cDLE® Pilot Plant

    cDLE® Pilot Plant Sorption Contactors Desorption Contactors December 2023 Direct Lithium Extraction 2023 18

  19. Slide 19: Commercial Plants

    Commercial Plants DRC uranium – 1,000m3/h Oman sulphate antimony – 50m3/h December 2023 Direct Lithium Extraction 2023 19

  20. Slide 20: Commercial Plants

    Commercial Plants Odos China nitrate – 250m3/h Fosterville Australia sulphate – 100m3/h December 2023 Direct Lithium Extraction 2023 20

  21. Slide 21: Render of typical cDLE® plant

    Render of typical cDLE® plant Barren Brine Lithium Desorption Tanks Contactors Lithium Sorption Train 1 Contactors Lithium Brine Lithium Desorption Feed Tanks Train 2 Contactors Direct Lithium Extraction 2023 21

  22. Slide 22: cDLE® Downstream – Clean-IX® & HIROX®

    cDLE® Downstream – Clean-IX® & HIROX® Lithium cDLE® Eluent Purification concentrate B using Clean-IX® Removal Ca/Mg Ca/Mg • Divalent ion removal Removal Boron Removal • Boron removal IDA Resin selective HIROX® IDA Resin anion • Reverse Osmosis exchange Concentration • Divalent ion removal Carbonatio

  23. Slide 23: cDLE® Upstream – Graphene Membranes

    cDLE® Upstream – Graphene Membranes TOC Brine Pre-treatment using Graphene Membranes • TOC removal • Flux 100LMHb (@4bar) Graphene • MWCO>90% @ 800Daltons Membranes • Low to no salt rejection • Fouling resistant • Chlorine resistant Lithium Brine cDLE® Circuit Operation Pressure 2 bar Water Recovery

  24. Slide 24: Corporate Headquarters

    Corporate Headquarters 402-1505 West 2nd Ave, Vancouver, BC, V6H 3Y4, Canada Technology Headquarters 12/21 Howleys Rd, Notting Hill, VIC 3168, Australia Contact [email protected]

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