The recovery of cyanide from a gold mill solution containing high levels of
copper (400 mg/L to 900 mg/L) using the A VR process was evaluated. It was
determined that acidification to pH 2 to 3 provides a suitable balance bet
ween HCN generation, copper precipitation and acid consumption. A short pil
ot plant campaign showed that similar to 75% of the feed WAD cyanide was re
covered while the remainder precipitated along with copper upon acidificati
on. The acid consumption averaged 3.5 g H2SO4 per litre of solution. The co
pper precipitate, consisting mostly of CuCN and CuSCN, was readily separate
d from the solution by gravity. The volatilization of HCN in countercurrent
packed columns averaged 98.7% efficiency Reabsorption of HCN was practical
ly 100% in NaOH solutions and slightly lower in a lime slurry. Basic volati
lizer design parameters applicable to a large-scale operation were determin
ed, including the Henry's law constant and the mass transfer coefficient of
HCN gas.