Gold CIL: Leach, Adsorb, Elute, Electrowin — Where the Gold Goes Missing
Carbon-in-leach (CIL) combines leaching and adsorption in the same tanks, which protects dissolved gold from being re-adsorbed by carbonaceous ore. The flowsheet is well established, and most recovery losses come from a small number of predictable places.
Route
| Step | Equipment | Key parameter |
|---|---|---|
| 1. Grinding | Ball mill, cyclone | P80 75 µm for liberation |
| 2. Pre-aeration / leach | Agitated tanks, air sparging | pH 10.5–11, DO > 6 mg/L, CN 200–500 mg/L |
| 3. CIL adsorption | 6–8 tanks with carbon | Carbon 10–25 g/L, counter-current movement |
| 4. Elution | Column, hot caustic | 120–140 °C, 1–3% NaOH, 3–5 bed volumes |
| 5. Electrowinning | EW cell, steel wool cathodes | 3–5 V per cell, 60–80 °C |
| 6. Smelting | Furnace | Flux recipe for doré |
Where gold is lost
Preg-robbing. Carbonaceous ore adsorbs gold from solution before carbon does. Test for it; the answer is usually a pre-oxidation step or a different flowsheet entirely.
Carbon fouling. Oils, flotation reagents and scale block carbon pores. A carbon regeneration kiln is not optional in a plant handling flotation concentrate.
Fine carbon. Carbon breaks down and reports to tailings with gold on it. Screen the carbon and recover fines; it is one of the cheapest wins available.
Short-circuiting in tanks. Poor interstage screening lets pulp bypass contact. Check screen condition and tank baffling.
Pilot scale
A 50–200 L CIL train running several cycles gives you leach kinetics, carbon loading and elution behaviour on your actual ore. Bottle-roll tests give kinetics; they do not give you the adsorption profile that decides tank count.
Send the head grade, ore mineralogy and any preg-robbing test result, and we will size the leach and CIL train.