US4501721A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Leaching and washing a flocculated slurry having a fiber content
Assignee: Andritz Inc
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Filing: 1983-06-10
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Granted: 1985-02-26
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Expires: 2003-06-10
Abstract
Abstract Particlized mineral material, such as gold ore, silver ore, or coal, is subjected to a leaching process in a manner to maximize treatment effectiveness even when the particlized mineral material contains small fines. The material is slurried with a flocculating material and fibers, such as cellulosic fibers, fiberglass fibers, or ceramic fibers, and a liquid, and then is passed to the top of a leaching reactor. The slurry is continuously passed downwardly in the reactor while the leaching liquid, such as a cyanide solution, is passed counter-current to the slurry. Leaching liquid is removed from the top of the leaching reactor by a stilling well, and then passed through a carbon adsorber and reintroduced into the reactor. Leached slurry is passed to a continuous washing station being utilized as a slurrying liquid for the particlized mineral material.
Inventors
- 👤 Michael I. Sherman
- 👤 Carl L. Elmore
- 👤 Robert J. Brison
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 22:31
CPC Classifications
C; C22; C22B; C22B11/00; C22B11/08; B; B01; B01D; B01D11/00; B01D11/02; B01D11/0215; B01D11/0253; B01D11/0257; B01D11/028; B01D11/0284; B03; B03D; B03D3/00; B03D3/06; C22B11/04; B01D2011/002
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
155 words
A method of removing metal from a particlized metal bearing ore, utilizing a treatment vessel, comprising the steps of: (a) mixing the particlized ore with a liquid to form a liquid slurry, a flocculating material so as to lock the particlized ore in a stable network in the slurry, and fibers so as to facilitate locking of the particlized ore in a stable network in the slurry; (b) continuously passing the slurry downwardly in the vessel; (c) continuously passing a leaching liquid, capable of leaching the metal to be removed from the metal bearing ore, upwardly in the vessel, countercurrent to the slurry passage, to remove metal from the ore in the slurry; (d) continuously removing the treatment slurry from a bottom portion of the vessel; (e) continuously removing pregnant leaching liquid, with metal removed from the ore, from a top portion of the vessel; and (f) continuously washing the slurry removed in step (d).
Claim 2
Independent Claim
155 words
A method of removing metal from a particlized metal bearing ore, utilizing a treatment vessel, comprising the steps of: (a) mixing the particlized ore with a liquid to form a liquid slurry, a flocculating material so as to lock the particlized ore in a stable network in the slurry, and fibers so as to facilitate locking of the particlized ore in a stable network in the slurry; (b) continuously passing the slurry downwardly in the vessel; (c) continuously passing a leaching liquid, capable of leaching the metal to be removed from the metal bearing ore, upwardly in the vessel, countercurrent to the slurry passage, to remove metal from the ore in the slurry; (d) continuously removing the treatment slurry from a bottom portion of the vessel; (e) continuously removing pregnant leaching liquid, with metal removed from the ore, from a top portion of the vessel; and (f) continuously washing the slurry removed in step (d).
Claim 3
Dependent Claim
26 words
A method as recited in claim 1 wherein the flocculent is selected from the group consisting essentially of synthetic polymers of anionic, cationic, and nonionic types.
Claim 4
Dependent Claim
27 words
A method as recited in claim 1 wherein the fibers are selected from the group consisting essentially of cellulosic fibers, fiberglass fibers, ceramic fibers, and mixtures thereof.
Claim 5
Dependent Claim
26 words
A method as recited in claim 3 wherein the flocculent is selected from the group consisting essentially of synthetic polymers of anionic, cationic, and nonionic types.
Claim 6
Dependent Claim
23 words
A method as recited in claim 4 wherein the fibers comprise, by weight, between about 0.01 percent and 10 percent of the slurry.
Claim 7
Dependent Claim
22 words
A method as recited in claim 5 wherein the fibers comprise, by weight, between about 0.05 and 0.75 percent of the slurry.
Claim 8
Dependent Claim
18 words
A method as recited in claim 4 wherein the leaching liquid in step (c) is a cyanide solution.
Claim 9
Dependent Claim
23 words
A method as recited in claim 1 wherein the fibers comprise, by weight, between about 0.01 percent and 10 percent of the slurry.
Claim 10
Dependent Claim
22 words
A method as recited in claim 8 wherein the fibers comprise, by weight, between about 0.05 and 0.75 percent of the slurry.
Claim 11
Dependent Claim
56 words
A method as recited in claim 1 wherein step (f) is practiced utilizing a washing vessel, and by passing wash liquid upwardly in the vessel counter-current to slurry moving downwardly in the vessel, with spent wash liquid removed from a top portion of the vessel and washed slurry removed from a bottom portion of the vessel.
Claim 12
Dependent Claim
23 words
A method as recited in claim 1 consisting essentially of said steps (a)-(f), so that carbon addition to the slurry is not practiced.
Claim 13
Dependent Claim
87 words
A method as recited in claim 10 wherein said washing vessel comprises a first vessel, and wherein step (f) is practiced utilizing a second vessel substantially identical to the first vessel, the slurry outlet from the first vessel being connected to the slurry inlet to the second vessel, and the wash liquid inlet to the first vessel being connected to the wash liquid outlet from the second vessel; and wherein the wash liquid outlet from the first vessel is used as a liquid for practicing step (a).
Claim 14
Dependent Claim
18 words
A method as recited in claim 1 wherein the leaching liquid in step (c) is a cyanide solution.
Claim 15
Dependent Claim
39 words
A method as recited in claim 13 comprising the further step of: (g) continuously passing pregnant liquid withdrawn in step (e) through a carbon adsorbing device, and reintroducing the liquid into the vessel as leaching liquid for step (c).
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-02-26 | 1988-08-27 | 1989-02-26 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-02-26 | 1992-08-27 | 1993-02-26 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-02-26 | 1996-08-27 | 1997-02-26 | $7700.00 | Window Closed / Lapsed |