CIL vs CIP: Choosing the Right Carbon for Gold Extraction
Release time:
25-11-05
Source:
The Core Difference: Leaching vs. Adsorption Sequence
The fundamental difference lies in the timing of leaching (dissolving the gold with cyanide) and adsorption (capturing the dissolved gold onto activated carbon).
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CIP (Carbon-in-Pulp): This is a two-step sequential process.
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Leaching: The ground ore slurry enters a series of agitated tanks where cyanide is added and the gold is dissolved. This is the “Leach Circuit.”
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Adsorption: The leached slurry then flows into a separate, subsequent series of tanks called the “Adsorption Circuit.” Here, activated carbon is added to capture the dissolved gold.
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CIL (Carbon-in-Leach): This is a combined process.
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Leaching and adsorption occur simultaneously in the same tank series. Activated carbon is present from the beginning, adsorbing the gold as it is being dissolved by the cyanide.
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Detailed Comparison Table: CIL vs. CIP
| Feature | CIP (Carbon-in-Pulp) | CIL (Carbon-in-Leach) |
|---|---|---|
| Process Flow | Sequential: Leaching → Adsorption | Combined: Leaching + Adsorption simultaneously |
| Number of Tanks | Higher (separate trains for leaching and adsorption) | Lower (single train for both functions) |
| Plant Footprint | Larger | Smaller |
| Capital Cost (CAPEX) | Higher (more tanks, more inter-tank pumps) | Lower (fewer tanks, simpler layout) |
| Residence Time | Longer overall, as steps are separate | Shorter overall, as processes are concurrent |
| Efficiency with “Preg-Robbing” Ores | Poor. Gold dissolved in the leach circuit can be lost to naturally occurring carbonaceous material before it reaches the adsorption circuit. | Excellent. Activated carbon is present to competitively adsorb the gold immediately, “winning” against the preg-robbing material. |
| Control & Optimization | Easier. Leaching and adsorption can be optimized independently (e.g., leach chemistry, carbon transfer rates). | More Complex. Parameters affect both leaching and adsorption, making fine-tuning trickier. |
| Risk of Fouling/Passivation | Lower risk of carbon fouling, as it’s only exposed to a fully leached solution. | Higher risk. Carbon is exposed to fresh ore and reagents for longer, which can lead to blinding or poisoning. |
| Flexibility | More flexible for complex ores where leach conditions need to be tightly controlled. | Less flexible; the process is “set” for the combined reaction. |
Key Factors for Choosing the Right Process
The choice isn’t about which is “better” in a vacuum, but which is more suitable for your specific ore body and project economics.
1. Ore Type: The Decisive Factor for “Preg-Robbing”
This is often the single most important consideration.
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Choose CIL if your ore is “preg-robbing.” Preg-robbing ore contains naturally occurring carbonaceous material (shale, graphite, etc.) that acts like activated carbon. It “robs” the pregnant solution of its gold by adsorbing it, making it unrecoverable.
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CIL Solution: By adding activated carbon immediately, you provide a more efficient and attractive surface for the dissolved gold than the preg-robbing material. The commercial carbon “out-competes” the native carbon, protecting your gold recovery.
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Choose CIP for non-preg-robbing ores. If your ore is “clean” and free of carbonaceous material, CIP is often the preferred choice. It allows for optimal leaching conditions without the complicating presence of carbon.
2. Capital and Operating Costs (CAPEX & OPEX)
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Choose CIL for lower CAPEX. Fewer tanks, less piping, and a simpler layout mean a lower initial investment. This makes CIL attractive for smaller projects or in locations where capital is a major constraint.
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CIP may have advantages in specific OPEX areas. Because the carbon is only in the adsorption circuit, it can have a longer life and require less frequent regeneration than in a CIL circuit, where it is subjected to harsher conditions for longer.
3. Operational Simplicity and Control
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Choose CIL for operational simplicity. The single-train process is easier for operators to manage on a day-to-day basis, with fewer moving parts and transfer points.
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Choose CIP for advanced process control. If you have a complex ore that requires precise control over leach kinetics, pH, and cyanide levels, CIP allows you to fine-tune the leach circuit independently of the adsorption circuit. This can be critical for maximizing recovery from refractory or variable ores.
Summary: When to Use Which?
| Scenario | Recommended Process | Rationale |
|---|---|---|
| Ore contains carbonaceous (preg-robbing) material | CIL | Protects gold recovery by providing a competitive adsorbent. |
| Simple, free-milling ore with no preg-robbing | CIP | Allows for optimized, independent leaching and adsorption. |
| Tight capital budget (CAPEX constraint) | CIL | Lower initial cost due to fewer tanks and simpler design. |
| Complex ore requiring precise leach control | CIP | Enables independent optimization of leaching parameters. |
| Space is a major constraint | CIL | Smaller physical footprint. |
| Desire for operational simplicity | CIL | Single train is easier to operate and maintain. |
Conclusion
There is no universal winner. The history of gold processing has seen a shift towards CIL becoming more dominant, primarily because:
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Many new gold discoveries are in deposits with some degree of preg-robbing character.
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The lower capital cost of CIL is highly attractive for project economics.
However, CIP remains a robust, efficient, and often superior process for well-understood, non-preg-robbing ores where maximum recovery through precise control is the primary goal.
The final decision must be based on comprehensive metallurgical test work that characterizes the ore’s leaching kinetics, preg-robbing potential, and response to both CIL and CIP flowsheets.
CTC
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