
|
Parameter |
Acid |
AmmLeach™ |
|
Mineralogy |
Oxides, carbonates, silicates, some sulphides |
Almost any – dependant upon curing stage |
|
Curing |
Concentrated H 2 SO 4 |
Tailored to ore mineralogy |
|
Selectivity |
Low- iron, manganese, calcium and silica are likely problems |
High- no iron, manganese, calcium or silica dissolution |
|
Rate of extraction |
Limited by acid strength and diffusion |
Ammonia concentration in leach solution matched to leaching rate |
|
Recovery |
80% of leachable |
70-80% in 130 days typical |
|
Heap lifetime |
55-480 days |
~80-130 days typical |
|
Sulphate precipitation |
Reduced permeability in heap, break down of clays and plant scaling due to precipitation of gypsum and jarosite |
Calcium and iron solubilities too low for precipitation, also low sulphate levels in leach solution |
|
Parameter |
Acid |
AmmLeach™ |
|
Leachate consumption |
Depends upon carbonate content
3.7-27 kg/t reported |
Depends on concentration used,
field trials show less than 1kg/t |
|
Safety |
Concentrated acid required |
Gaseous ammonia main hazard, on ‑ demand systems using hydrolysis of urea minimise transport risks |
|
Precious metals |
Heap to be neutralised before cyanidation |
Neutralisation not required, potential for simultaneous recovery using thiosulphate or sequential leaching using cyanide |
|
Mine closure |
Heap requires washing, neutralisation and long term monitoring to avoid AMD |
Heap can be washed and left, residual ammonia acts as fertiliser for vegetation regrowth, minimal likelihood of AMD. |