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Gold ore is processed in a sequence that turns blasted rock into a gold-silver doré bar: the mine delivers run-of-mine (ROM) ore, crushers and mills liberate the gold, and gravity or flotation may remove particular gold-bearing fractions. Most of the remaining stream is leached with sodium cyanide, then dissolved gold is recovered on activated carbon, stripped, plated by electrowinning, filtered, dried and smelted with fluxes. The doré bar is an intermediate product sent to a refinery, not normally 99.99% pure bullion.
Every plant changes this sequence to suit its ore. Mineralogy, gold liberation, hardness, sulphide content, deleterious elements, water balance, tailings design and regulatory requirements determine whether a circuit uses gravity, flotation, carbon-in-pulp (CIP), carbon-in-leach (CIL), or a combination.
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1. From mine face to plant feed
Mining, blasting and haulage
Open-pit drill-and-blast operations and underground stoping break the orebody into rock that can be loaded and hauled. The project technical reports cited for this process treat ROM ore as the plant feed; the exact mining method, truck fleet, underground layout and haul distances are project-specific. Trucks deliver the material either to the primary crusher or to a ROM stockpile that provides short-term blending and feed control.
Why blending matters
Ore arriving at a mill is not chemically uniform. Operators may blend harder and softer zones, different sulphide contents or different grades so the plant sees a manageable range of hardness and leach behavior. The blend affects crusher throughput, mill power, reagent demand, residence time and the amount of gold that can be recovered.
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2. Crushing and coarse-ore storage
Primary crushing
A jaw or gyratory crusher breaks ROM rock into smaller pieces. The objective is not yet to make sand; it is to produce a consistent feed for the grinding circuit while removing the very large rocks that mills cannot accept. Conveyors move the crushed material to a coarse-ore stockpile.
Stockpile and reclaim
The stockpile decouples the mine from the mill. Mine trucks can keep dumping while the mill receives a controlled, metered stream through reclaim feeders and conveyors. The Tocantinzinho project design specifically places primary crushing before a coarse-ore stockpile and reclaim system.
3. Grinding and classification liberate the gold
SAG and ball mills
Crushed ore is mixed with process water and reduced further in a semi-autogenous grinding (SAG) mill, a ball mill, or both. Grinding exposes gold grains that were locked inside quartz, sulphide minerals or other gangue. The required fineness is an ore-specific compromise: finer grinding can improve liberation but consumes more energy and can create slurry-handling or recovery problems.
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Hydrocyclones separate particles by size. Coarse underflow returns to the mill for more grinding, while the fine overflow advances to recovery. In the Tocantinzinho design, the final grinding product has a P80 of 125 micrometres, meaning 80% of the classified product passes a 125 µm size. That figure is a project design parameter, not a universal target for gold mines.
4. Optional recovery before whole-ore leaching
Gravity concentration for coarse, free gold
If grinding releases relatively coarse gold, centrifugal concentrators or other gravity equipment can recover it from the circulating slurry. The gravity concentrate may receive intensive cyanidation and separate electrowinning. Pulling out this high-grade fraction early can reduce the load on the main leach circuit, but gravity is useful only when the ore actually contains recoverable, liberated gold of suitable size and density.
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Flotation for sulphide-associated gold
When gold is hosted by sulphide minerals, flotation can produce a sulphide concentrate. The concentrate may be reground and cyanide-leached separately, while the flotation tailing follows another treatment route. Tocantinzinho explicitly includes a two-stage sulphide flotation circuit. Flotation is therefore a mineralogical decision, not a mandatory step in every flowsheet.
Whole-ore leach versus concentrate leach
A whole-ore leach sends the appropriate ground stream to cyanidation. A concentrate-leach arrangement first upgrades sulphide minerals by flotation, then treats a smaller mass at finer grind or under different reagent conditions. The choice depends on gold liberation, sulphide behavior, hardness, grinding energy, cyanide consumption and the performance demonstrated by metallurgical test work.
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Conditioning the slurry
Some plants condition the ground slurry with air or oxygen before cyanidation. Pre-aeration can establish the chemical environment needed for the selected leach conditions, but its use and duration depend on the ore and test results.
How cyanidation dissolves gold
Sodium cyanide converts exposed metallic gold into a soluble gold-cyanide complex in an alkaline, oxygenated slurry. Agitated tanks provide mixing and residence time so the reagent can contact newly liberated gold. The cyanide concentration, oxygen supply, pH control, solids density and tank volume are selected from metallurgical testing and observed ore behavior; there is no single recipe that applies to every deposit.
Cyanide is a hazardous industrial reagent. Mine-scale cyanidation requires engineered tanks, lined areas, monitoring, trained personnel, emergency systems and a permitted water and tailings-management plan. It is not a household or small-shop process.
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Residence time is a design value
The Tocantinzinho feasibility study (2022) specifies 36 hours of CIL residence time. That is a parameter for that project’s ore and plant design, not a universal requirement. A different ore may need more or less time, or a different pretreatment, to reach its recovery target.
6. CIP and CIL: what the terms actually mean
Both circuits use activated carbon to adsorb dissolved gold complexes, but they place adsorption in relation to leaching differently.
| Arrangement | Where carbon contacts the slurry | Typical process distinction |
|---|---|---|
| Carbon-in-pulp (CIP) | In a separate adsorption train after leach tanks | Leaching and adsorption are staged as distinct sections |
| Carbon-in-leach (CIL) | In the leach train while cyanidation is still taking place | Leaching and adsorption occur concurrently in the same sequence of tanks |
In either arrangement, screens retain the carbon while slurry flows onward. Carbon moves counter-currently through the tanks so the freshest carbon meets the lowest-gold solution and the most heavily loaded carbon is removed for stripping. The selected configuration, number of tanks and residence time depend on ore kinetics, soluble losses, carbon activity and plant design.
7. Recovering gold from loaded carbon
Screening and acid washing
Loaded carbon is screened out of the adsorption circuit. An acid wash removes carbonate scale and other foulants that block adsorption sites. The wash chemistry and handling system are designed to avoid sending unwanted dissolved metals into the subsequent strip solution.
Elution produces a pregnant solution
During elution, a hot, chemically controlled solution strips the adsorbed gold from the carbon. The result is a gold-rich pregnant eluate. The carbon is not discarded: thermal regeneration restores adsorption capacity so it can return to the CIP or CIL circuit.
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8. Electrowinning makes cathode sludge
The pregnant eluate enters electrowinning cells. An electrical current plates metallic values onto cathodes, producing a sludge that contains gold along with silver and other metals carried through the process. Electrowinning is therefore a concentration step, not final refining to investment-grade purity.
Aura Minerals’ 2025 Era Dorada Gold Project technical report summarizes this section as: “Gold refining – Gold electrowinning (sludge production), filtration, drying and smelting to produce gold doré.” The wording describes the plant sequence; it does not imply that the resulting bar is refinery-grade bullion.
Independent reader supportYour contribution helps us test, update, and keep practical guides available for everyone.9. Filtering, drying and smelting the doré bar
Preparing the sludge
Operators filter the cathode sludge to remove liquid and then dry it. The dry material is weighed and sampled so the plant can account for gold, silver, moisture and other contained metals.
Fluxing and melting
Fluxes are blended with the dried sludge to help collect precious metals and separate a molten slag phase. In a furnace, the charge melts and is poured into molds. The cooled product is a doré bar, an intermediate gold-silver alloy that may contain copper, iron, lead or other metals depending on the ore and circuit.
Why doré is not pure bullion
Doré composition and fineness are plant-specific and must be established by assay. The available project reports do not support one global recovery percentage, cost benchmark or doré-fineness statistic. The bars are shipped to an off-site refinery, where further chemical or electrolytic treatment separates gold, silver and residual impurities to the buyer’s specification.
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10. Cyanide destruction and tailings management
Detoxifying residual cyanide
After soluble gold has been recovered, the remaining slurry can still contain cyanide and metal-cyanide complexes. Plants detoxify or destroy residual cyanide before discharge to the tailings system, using a process selected for the site’s chemistry and permit limits.
Thickened, filtered or pumped tailings
Tailings are the finely ground solids and process water left after recovery. A plant may thicken the slurry, filter it to produce a drier cake, or pump it to a tailings-storage facility. Recovered water is commonly returned to the process circuit, reducing fresh-water demand and limiting the volume sent to storage. The choice affects pumps, filtration energy, dam or dry-stack design, seepage controls and closure obligations.
11. Published design figures and what they mean
| Project or source | Figure | How to interpret it |
|---|---|---|
| Tocantinzinho Project technical report (2019) | 4.3 million tonnes per year nominal mill capacity | Designed annual ore-throughput capacity for that project |
| Tocantinzinho Project technical report (2019) | 174,000 ounces planned annual gold production | Planned output for the project design, not a universal mine result |
| Tocantinzinho Project technical report (2019) | 125 µm final grinding P80 | Specified product-size target for that grinding circuit |
| Tocantinzinho Feasibility Study (2022) | 36 hours CIL residence time | Design residence time for the study’s ore and circuit |
12. Why two gold mines use different flowsheets
Engineers choose a flowsheet from test work rather than copying a neighboring operation. The decisive questions include:
- Mineralogy and liberation: Is gold free after grinding, locked in sulphide minerals, or associated with refractory phases?
- Particle size and hardness: How much grinding energy is needed, and does finer grinding improve recovery enough to justify the power and equipment?
- Gravity response: Is there enough coarse, liberated gold to justify a gravity concentrator and intensive cyanidation loop?
- Flotation response: Can sulphide flotation make a stable, high-value concentrate, and can that concentrate be leached economically?
- Leach behavior: Does the ore consume cyanide or oxygen, foul carbon, or require pre-aeration and other conditioning?
- Water and tailings: Can the site recycle water, thicken or filter tailings, and meet cyanide and seepage limits?
- Capital and operating complexity: Will extra crushing, flotation, regrinding, detoxification or filtration provide enough additional payable metal to justify the cost and control burden?
13. Common misconceptions and practical limits
“Every mine uses gravity and flotation”
No. Gravity is selected for coarse free gold, while flotation is selected when sulphide minerals carry enough gold to warrant concentration. Many ores proceed from grinding directly to leaching; others use one or both optional circuits.
“CIL always takes 36 hours”
No. Thirty-six hours is the Tocantinzinho feasibility-study design value. Residence time is established by leach-kinetics testing, tank volume, throughput and the required recovery.
“The first bar is 99.99% gold”
No. Smelting produces doré, an intermediate gold-silver bar. Assay determines its actual composition, and an external refinery performs the final separation.
“A recovery percentage or cost can be applied to every orebody”
No universal recovery, cost or fineness statistic is established by the cited material. Metallurgy, grade, liberation, deleterious elements, energy prices, water management and plant practice change the result from one project to another.
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Quick Recap
14. The complete mine-to-doré sequence
- Mine and haul ROM ore to a crusher or stockpile.
- Crush the rock and reclaim it at a controlled rate.
- Grind in SAG and/or ball mills and classify with hydrocyclones.
- Recover coarse free gold by gravity when test work justifies it.
- Float sulphide minerals, regrind the concentrate and leach it when the ore requires that route.
- Condition the slurry with air or oxygen where the selected metallurgy calls for pre-aeration.
- Leach exposed gold with sodium cyanide under controlled conditions.
- Adsorb dissolved gold on activated carbon in a CIP or CIL arrangement.
- Screen, acid-wash, elute and thermally regenerate the carbon.
- Electrowin the pregnant eluate to make cathode sludge.
- Filter and dry the sludge, add fluxes, and smelt it into doré.
- Detoxify residual cyanide and thicken, filter or pump tailings while recovering process water.
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