Three hydrometallurgical processes for industrial wastes treatment are
presented. ?The main separation techniques are: solvent extraction, l
eaching-precipitation, electro-oxidation, and ion exchange. Recovery o
f gold from solid wastes generated in the electronic and jewellery ind
ustries consists of thermal degradation, two-stage leaching with nitri
c acid solution to remove silver and other metals and then with aqua r
egia to dissolve gold, selective solvent extraction of gold with dieth
yl malonate, and reduction of gold from the organic phase. Vanadium re
covery from residue ashes after burning heavy oil fractions consists o
f alkaline leaching of vanadium, filtration, neutralization of sodium
vanadate solution, precipitation of ammonium metavanadate, drying of t
he precipitate, and adsorption of the remaining vanadium from the filt
rate on an anionite. From the remaining ashes nickel is recovered usin
g acidic leaching, filtration, precipitation of ammonium-nickelous sul
phate, filtration, and drying. The third process concerns processing o
f electroplating sludges and waste waters containing chromium and copp
er. The waste waters are electro-oxidized to transform Cr(III) into ch
romate. Then metal cations are separated on a cationite. The purified
electroplating baths are recycled directly to electroplating; other so
lutions are first concentrated using anionite, followed by sodium chro
mate eluate conversion into concentrated chromic acid solution. The sl
udges accumulated from waste water processing by hydroxide precipitati
on are re-dissolved in chromic acid solution generated progressively b
y circulation between the dissolving and electro-oxidation steps. The
concentrated chromic acid solution obtained is purified on the cationi
te and recycled.