US2010181205A1PendingUtilityA1
Method for treating waste containing precious metals and device for implementing said method
Est. expiryOct 20, 2026(~0.2 yrs left)· nominal 20-yr term from priority
Inventors:Christian Thpmas
Y02P10/20C22B 11/021C22B 7/001B03B 9/061
20
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Claims
Abstract
The application relates to a method for treating waste containing precious metals, said method comprising the following successive steps: the waste is brought into contact with a composition based on molten lead; the mixture obtained is skimmed; and the skimmed mixture is refined by electrolysis in such a way as to recover the precious metals. The application also relates to a waste treatment installation for implementing said method.
Claims
exact text as granted — not AI-modified1 . A method for treating waste containing precious metals, comprising the following successive steps:
contacting the waste with a molten lead-based composition; skimming the obtained mixture in order to recover supernatant materials; and refining the skimmed mixture by electrolysis so as to recover the precious metals.
2 . The method according to claim 1 , wherein, in the skimming step, residues are recovered which are treated by:
contacting the residues with a second molten lead-based composition; skimming the obtained mixture; and recovering the skimmed mixture in order to provide at least one portion of the molten lead-based composition of claim 1 .
3 . The method according to claim 1 , wherein the step of refining the skimmed mixture comprises the following sub-steps:
casting the skimmed mixture into anodes; electrolysis of a fluorosilicic acid solution by using said anodes; and recovering anodic sludges containing the precious metals.
4 . The method according to claim 3 , comprising before, simultaneously or after the step of recovering anodic sludges, the step of:
recovering lead and optionally tin cathode deposits in order to provide at least one portion of the molten lead-based composition and/or of the second molten lead-based composition.
5 . The method according to claim 3 , wherein the step of refining the skimmed mixture comprises, after the sub-step of recovering anodic sludges, the following additional sub-steps:
melting the recovered anodic sludges in the presence of oxygen; skimming the molten anodic sludges; and casting the molten and skimmed anodic sludges into ingots.
6 . The method according to claim 1 , wherein each molten lead-based composition comprises from 0 to 50% of tin.
7 . The method according to claim 1 , comprising, prior to the step of contacting the waste with a molten lead-based composition, the step of:
extracting copper from the waste by selective dissolution.
8 . The method according to claim 7 , wherein the copper extraction step comprises the following sub-steps:
selectively dissolving the waste in the presence of sulfuric acid, iron sulfate and oxygen; treating the obtained solution by filtration and/or electrolysis and/or precipitation; recovering copper on the one hand and other metal impurities on the other hand.
9 . The method according to claim 7 , comprising, prior to the copper extraction step, the following steps:
combustion of the waste by pyrolysis, producing carbonaceous gases; and optionally post-combustion of the carbonaceous gases.
10 . The method according to claim 1 , further comprising a preliminary step of milling the waste and/or analyzing the milled waste.
11 . The method according to claim 1 , wherein the precious metals comprise one or more metals selected from gold, silver, platinum, palladium, rhodium, ruthenium, iridium, osmium and mixtures thereof.
12 . The method according to claim 1 , wherein the waste is selected from catalytic exhaust mufflers and electronic waste such as electronic cards.
13 . The method according to claim 1 , wherein more than 90% by mass of the precious metals contained in the waste are recovered.
14 . The method according to claim 1 , wherein the supernatant materials comprise ceramics, glass fibers and/or ferrite.
15 . An installation for treating waste containing precious metals, the installation comprising:
at least one lead covering container; a molten lead-based composition feed line, connected to the inlet of the lead covering container; a pre-treated materials feed line, connected to the inlet of the lead covering container; a skimmer associated with the lead covering container; a skimmed mixture withdrawal line connected to the outlet of the lead covering container; a refiner operably refining the skimmed mixture by electrolysis fed by the skimmed mixture withdrawal line; and a precious metals withdrawal line, connected to the outlet of the refiner.
16 . The treatment installation according to claim 15 , further comprising:
a skimming residues withdrawal line, connected to the outlet of the skimmer; at least one additional lead covering container, fed by the skimming residues withdrawal line on the one hand and by an additional molten lead-based composition feed line on the other hand; an additional skimmer associated with the additional lead covering container; and an additional skimmed mixture withdrawal line, connected to the outlet of the additional lead covering container and feeding the molten lead-based composition feed line.
17 . The treatment installation according to claim 15 , wherein the refiner of the skimmed mixture by electrolysis further comprises:
means for casting anodes; Betts electrolysis means; and means for recovering anodic sludges.
18 . The treatment installation according to claim 17 , wherein the refiner of the skimmed mixture by electrolysis further comprises:
means for recovering lead-tin, feeding the additional molten lead-based composition feed line.
19 . The treatment installation according to claim 15 , further comprising:
a copper extractor, one outlet of which is connected to the pre-treated materials feed line, and a primary materials feed line, connected to the inlet of the copper extractor.
20 . The treatment installation according to claim 19 , wherein the copper extractor further comprises:
at least one selective dissolution container, fed by the primary materials feed line; a depleted electrolyte feed line, connected to the inlet of the selective dissolution container; electrolysis means; means for transferring rich electrolyte, connecting the selective dissolution container to the electrolysis means; means for stripping the cathodes; and means for recycling depleted electrolyte, connected to the outlet of the electrolysis means.
21 . The treatment installation according to claim 19 , further comprising:
a pyrolysis oven acting on the waste, connected to the outlet of the primary materials feed line; a waste feed line feeding the pyrolysis oven and optionally a gas exhaust line at the outlet of the pyrolysis oven and feeding a post-combustion chamber.
22 . The treatment installation according to claim 15 , further comprising:
milling and analysis means fed by a raw waste feed line and feeding the waste feed line.Join the waitlist — get patent alerts
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