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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Electrowinning of gold copper ores (5 replies and 3 comments)

D
Metals Guy
6 years ago
Metals Guy 6 years ago

Hie guys.

I am having problems with the amount of copper associated with our ore. The copper content is not high enough for economic recovery but its high enough to cause problems in our CIP circuit and electrowinning. A typical elution would produce about 4kgs of gold and 5kgs of copper. The copper makes it difficult to strip the gold off the steel mesh cathodes. Which would be the best stage to eliminate copper, during cyanidation, adsorption or electrowinning. And how do i go about this. Please help. Thank you for in advance

F
Siddiquf
6 years ago
Siddiquf 6 years ago

What is the ore mineralogy of copper? Is it oxide or sulphide type mineral/s?

T
Todd H
6 years ago
Todd H 6 years ago

Hello - this is Todd Harvey from Global Resource Engineers

Can you answer a couple of questions on the process for me?:

  1. What type of elution circuit are you using?
  2. What are the main copper minerals?
  3. Do you have assay data on how much Cu is being extracted?
  4. What are your solution grades coming out of the leach circuit - Au, Ag, Cu, Fe - free/total cyanide, pH
  5. What is your cyanide concentration target - in the circuit and in the tails?
  6. Do you add cyanide stagewise or all in the first leach tank?
  7. Is your carbon activity impacted by the copper - what does your activity profile look like in the CIP tanks and after strip/regeneration?

There are a couple of things to consider here:

  1. Avoid mining the copper rich materials if possible - this may not be possible of course but certainly it would help - cyanide consumption would go down considerably and EW would be easier.
  2. Adding cyanide stagewise in smaller concentrations can help reduce the driving force reducing copper dissolution and cyanide consumption.
  3. Acid carbon washing does not generally reduce the copper prior to elution.  It actually can make it harder to elute.  A cold caustic cyanide prewash can remove the copper and this is a good option and you can install a small Cu EW circuit to remove the copper from the eluant and recycle it.  You may be able to use iron precipitation to remove the copper as well. I would recommend some simple test work to design a new wash procedure.
  4. The adsorption of copper cyanide complexes on carbon is highly pH dependent.  If you can raise you leach/CIP pH at or above 10.6 your copper adsorption will fall dramatically.  You will now have dissolved copper remaining in solution that may have to be removed.

If you need more advice fee free to contact me.  I can help with test work, design etc...

Regards

Todd

Todd Harvey - Global Resource Engineering http://www.global-resource-eng.com

D
Metals Guy
6 years ago

Thank your Mr harvey

1.we are using AARL elution circuit
2.Chalcopyrite is the major copper mineral
3.The last time i checked our elution assays, Au assayed 63ppm and copper 81ppm
5.Cynaide target is 300ppm and tails 80ppm
6. We add cyanide in the first tank
Question 4 and 7 i will have to compile the data.

C
Craig M
6 years ago
Craig M 6 years ago

I believe you could affect the copper in several stages. I published a paper in SMME preprint number 93-230 regarding control of copper in carbon adsorption and gold recovery circuits. In that paper it is described how cyanide addition in the adsorption circuit can force a large amount of copper off from the carbon, and also a 'cold cyanide strip' process of removing copper from the carbon, before stripping the gold and silver. Lastly the selective voltage control in electrowinning can reject copper in the deposition onto cathodes. Preprint # 93-230, Ttitle "Control of Copper in Carbon Adsorption and Gold Recovery Circuits - American Girl Mining Experience". I worked closely with an industry carbon expert, Rick Follis in making the plans and chemistry changes and accomplishing much copper reduction in the circuit.

D
Metals Guy
6 years ago

thank you Craig

M
mohammed elhadi
6 years ago
mohammed elhadi 6 years ago

Morning

Leaching: you need to change this ore to oxides by roasting(difficult) , maybe use washing by water ,Increase lime,blending with another ore by different ratio {you need make a lot of tests).

Adsorption: If you find a lot of copper in preg-solution and sent to carbon unit you can do {cold stripping) after finish from adsorption ..

REGARDS

D
Metals Guy
6 years ago

Thanks Mohammed

G
Teggry
6 years ago
Teggry 6 years ago

MAte, I had a similar problem from Heap leach solutions. We had a Zadra circuit and found cold stripping the carbon on a first run and then standard hot strip on a second run eradicated a lot of the copper.


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