- To participate in the 911Metallurgist Forums, be sure to JOIN & LOGIN
- Use Add New Topic to ask a New Question/Discussion about Hydrometallurgy.
- OR Select a Topic that Interests you.
- Use Add Reply = to Reply/Participate in a Topic/Discussion (most frequent).
Using Add Reply allows you to Attach Images or PDF files and provide a more complete input. - Use Add Comment = to comment on someone else’s Reply in an already active Topic/Discussion.
Please join and login to participate and leave a comment.
I have a small ball mill ( 1 to 2 tph ) and plenty of oxide ore and I was looking at the feasibility of building a test small scale leaching circuit that could be run in a batch style to keep it as simple as possible.
My current idea is once the ore is milled to an appropriate size, it is mixed with water to chosen density and pumped into a couple of old agitated tanks I've sourced.
I thought then add lime to the tanks to get the pH up to around 10, then slowly mix/add by hand ( with a respirator ) the cyanide solution. Once it's all mixed the agitators are run, cyanide/pH levels monitored for 6 to 10 hours. For oxygen is it possible to use a simple bubbler setup or easier to just add a chemical agent?
Once it's leached I'm not sure of the easiest way to handle the pregnant slurry, I know in proper setup you'd have the carbon flowing in a counter current manner but I'm looking for a simpler way, I thought maybe just letting the tanks settle, maybe add a bit of flocculent then slowly decanting the water off the top and circulating it through some carbon columns I've also sourced, or my other idea is maybe it would be easier to just add the carbon in the tanks during the leaching process then just pump the slurry through a proper carbon screen. Once it's all collected then it can be washed and transported to a contractor for stripping.
For the tailings I was going to pump them into a lined pond then try and decant some water to reuse and then destroy the cyanide with either peroxide or hypochlorite, from what I gather hypochlorite is the cheapest/most powerful oxidant but will this still be too dangerous even if I up the pH of the tailings and use a full respirator when adding the hypochlorite?
Also I want to try and reuse water so I'm guessing I'll have to try and lower the chlorine level ( or just let it naturally degrade? ) before I reintroduce it to the circuit, also would there be issues flocculent levels recirculating?
My other idea is building a plant is perhaps too hard and I should sell the ball mill and buy agglomeration equipment and look at heap leaching it instead, but they sound almost too deceptively simple plus losing 40 to 50% recovery, has anyone had a good experience setting up a small pilot heap? The ore is pretty varied theres plenty of low grade ( 0.6 - to 0.8 g/t ) and and small sections of high grade ( 5 - 10g/t)