Hydrometallurgy: Leaching in Heap, Vat, CIL, CIP, Merrill–Crowe, SX Solvent Extraction

Hydrometallurgy: Leaching in Heap, Vat, CIL, CIP, Merrill–Crowe, SX Solvent Extraction

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Design copper agitated leach tanks? (3 replies)

7 years ago
Gombera 7 years ago

Dear Professionals,

what are important steps should I follow when I want to design copper agitated leach tanks?



7 years ago
Jorge 7 years ago
2 likes by David and Gombera

The first step is to perform a leaching testing program in the met lab to evaluate several parameters,

  • The effect of particle size on copper extraction
  • Effect of sulphuric acid on copper extraction
  • pH value
  • Optimum residence time
  • Slurry density
  • Ore types

Once you got the results from the testing program, it is important to determine the processing rate, for example 300 t/d. It is important to prepare a mine plan to know the different ore types that would be treated in the process plant. 

Other important aspect to evaluate is what to do with the pregnant solution, for example, produce a copper precipitate (copper cement). One more time, it is necessary to consider a testing program. Also, a solid-liquid separation should be included in the design, a CCD circuit is a good option.

Based on the optimum results from testing program and the processing rate, it is possible select the number of tanks, and the tank size. 

The study should consider a financial evaluation to take a final decision. 

7 years ago
hllopez 7 years ago
1 like by David

Designing a leach circuit should consider both ore-specific factors as well as factors involving the interaction between the ore and process equipment.

Achieving the optimum leach performance involves combining operating parameters, such as grind size, residence time, chemical conditions (reagent addition levels, temperature, etc.), most of which interact with each other. Determining the optimum process conditions should be the objective of any metallurgical testwork program. Processes that are either relatively straightforward or are well understood, such as cyanide leaching of “free milling” gold, can be characterised on the basis of laboratory scale testwork. However, more complex or novel processes will require progressive stages of testwork, from laboratory to continuous pilot plants, to prove up and optimise the process ahead of plant design.

Grind size is usually the key process parameter in a leach plant, as grinding represents the highest energy input and cost element in the overall process. Sufficient grinding is required to expose the target minerals to the leach solution; the optimum grind size can range from the order of 1mm for minerals such as potash down to less than 10 microns for refractory sulfide minerals. There is some scope to offset grind size against residence time and/or reagent levels; the grind size also has impacts on material handling, such as agitator power for coarse grind sizes, and downstream thickening and filtration for fine grind sizes.

The tank material of construction (e.g., carbon steel, stainless steel, other metal alloy or non-metallic) is a function of the chemical and physical interaction between the ore and the process equipment. Agitator design is determined by whether the aim of the agitator is to simply keep the material suspended or the need for efficient introduction of air/oxygen for the leach reaction.

The technical aspects of designing the leach circuit fall within the overall project design activities. Key aspects of the overall design picture include the initial definition process, process selection through testwork and simulation, cost estimation and financial analysis, leading to the final design, construction and commissioning.

Reference: http://www.srk.com/en/newsletter/metallurgy-mineral-processing/leach-circuit-design-principles

You may also check out this link which gives a lot of tips https://www.911metallurgist.com/blog/leaching-plant-design

Marshal Meru
7 years ago
Marshal Meru 7 years ago

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