Brine to Lithium Carbonate: Evaporation, Polishing and Carbonation
Brine processing is a concentration business: you remove water and unwanted ions until lithium chloride or sulphate is strong enough to precipitate carbonate. Compared with hard-rock routes there is no grinding or leaching, but impurity control is harder because everything in the brine concentrates with the lithium.
Route
| Step | Purpose | Equipment | Key parameter |
|---|---|---|---|
| 1. Pre-treatment | Remove Mg, Ca, sulphate | Lime/soda softening, IX | Mg < 10 mg/L before concentration |
| 2. Concentration | Raise Li to 15–25 g/L | Solar ponds or MVR/MEE | Recovery > 85%, control NaCl/KCl |
| 3. Boron / residual Ca-Mg | Polishing | Selective IX | B < 5 mg/L |
| 4. Carbonation | Precipitate Li₂CO₃ | Reactor with Na₂CO₃ dosing, 80–90 °C | Stoichiometric control, seeding |
| 5. Dewatering and drying | Product | Centrifuge, dryer | < 0.2% moisture |
Magnesium is the project killer
Brine with a high Mg/Li ratio consumes large amounts of lime and generates a lot of gypsum sludge. Projects that look attractive on lithium grade fail on reagent cost. Run the softening test on actual brine before committing to a route.
MVR or solar?
Solar ponds are cheap to operate and slow; MVR is capital-intensive and fast, and it needs stable power. For a pilot or a small plant, MVR with a crystallizer gives control and a predictable schedule. For large tonnage in the right climate, ponds still win on opex.
Why pilot data matters here
Brine composition varies between aquifers and between seasons. A pilot that runs the actual brine for several weeks gives you the real magnesium and sulphate behaviour, the evaporator fouling rate, and a carbonate product sample for qualification.
Send the complete brine analysis (Li, Na, K, Mg, Ca, SO₄, B, Cl) and target product grade, and we will size the evaporator and polishing train.