Patent US2008251A successfully refreshed from Google Patents.
Patent US4139432A successfully refreshed from Google Patents.
US4139432A
Expired / Lapsed
US
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Process for electrochemically recovering precious metals from ores
Assignee: Individual
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Filing: 1976-08-16
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Granted: 1979-02-13
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Expires: 1996-08-16
Abstract
Abstract An electrochemical process for rapidly achieving the recovery of precious metals such as gold and silver from their ores. The ore is formed into a slurry and combined with an electrolyte such as sodium cyanide and an alkaline substance such as sodium hydroxide to increase alkalinity to at least 0.01 equiv./liter. The ore slurry and electrolyte are placed in a recovery apparatus in direct touching contact with closely spaced large area anodic and cathodic electrodes, preferably spaced apart by a distance of about 1 cm. or less. A voltage is applied to the electrodes to produce a current density in the slurry of about 10 to 20 amperes per square meter, and the slurry is agitated to provide diffusion of the ore grains into electrical contact with the electrodes to promote precious metal dissolution. The agitation further transports precious metal complexes to the cathode where the precious metal is electrolytically precipitated and the complexing agent freed for further electrolytic dissolution of the precious metal. The foregoing process and recovery apparatus markedly improve the rate of recovery of precious metals from their ores, reducing recovery times in some instances to less than 10 minutes from the 3 to 24 hours required in conventional cyanidation processes for comparable precious metal extraction.
Inventors
- 👤 Hugh A. Ghiringhelli
- 👤 Kenneth S. Deffeyes
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 12:37
CPC Classifications
C; C25; C25C; C25C1/00; C25C1/20
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
191 words
A process for electrochemically treating ores to increase the rate of recoverability of precious metals electrolytically mobile therein, comprising: forming a slurry of the ore; mixing a cyanide complexing agent for the precious metal and the water soluble electroconductive catonic resin polyvinylbenzyltri-methylammonium chloride as an electrolyte in dilute concentrations suitable to provide mobility for the precious metal desired to be recovered with the ore slurry; placing the ore slurry and electrolyte into direct touching contact with both anodic and cathodic electrodes; applying a voltage across the electrodes effective to produce a current density in the ore slurry and electrolyte of about 10 to 20 amperes per square meter to dissolve the precious metal from the slurry; and agitating the ore slurry and electrolyte while the voltage is being applied and while in contact with the electrodes sufficiently to provide bulk diffusion of the ore grains in the slurry in a direction across the interelectrode space and to bring the grains into electrical contact with the electrodes to recover the metal by electrodeposition; whereby the dissolution rate of the precious metals in the ore is increased and their rapid recovery is facilitated.
Claim 2
Dependent Claim
191 words
A process for electrochemically treating ores to increase the rate of recoverability of precious metals electrolytically mobile therein, comprising: forming a slurry of the ore; mixing a cyanide complexing agent for the precious metal and the water soluble electroconductive catonic resin polyvinylbenzyltri-methylammonium chloride as an electrolyte in dilute concentrations suitable to provide mobility for the precious metal desired to be recovered with the ore slurry; placing the ore slurry and electrolyte into direct touching contact with both anodic and cathodic electrodes; applying a voltage across the electrodes effective to produce a current density in the ore slurry and electrolyte of about 10 to 20 amperes per square meter to dissolve the precious metal from the slurry; and agitating the ore slurry and electrolyte while the voltage is being applied and while in contact with the electrodes sufficiently to provide bulk diffusion of the ore grains in the slurry in a direction across the interelectrode space and to bring the grains into electrical contact with the electrodes to recover the metal by electrodeposition; whereby the dissolution rate of the precious metals in the ore is increased and their rapid recovery is facilitated.
Claim 3
Dependent Claim
21 words
A process for electrochemically treating ores as claimed in claim 1 further comprising recovering the precious metal electrolytically at the cathode.
Claim 4
Dependent Claim
26 words
A process for electrochemically treating ores as claimed in claim 1 wherein the interelectrode spacing is within a range of about 0.3 cm to 1.0 cm.
Claim 5
Dependent Claim
33 words
A process for electrochemically treating ores as claimed in claim 1 wherein the precious metal to be recovered is gold or silver and alkalinity of the slurry is at least about 0.01 equivalents/liter.
Claim 6
Dependent Claim
17 words
A process for electrochemically treating ores as claimed in claim 4 wherein the electrolyte comprises sodium cyanide.
Claim 7
Dependent Claim
33 words
A process for electrochemically treating ores as claimed in claim 1 wherein the electrodes have surface areas of about 0.1 to 1 square meter per ton of ore to be processed per day.
Claim 8
Dependent Claim
30 words
A process for electrochemically treating ores as claimed in claim 1 wherein the voltage applied to the electrodes is maintained sufficiently low to prevent emission of hydrogen at the cathode.
Claim 9
Dependent Claim
20 words
A process for electrochemically treating ores as claimed in claim 1 wherein a d.c. voltage is applied to the electrodes.
Claim 10
Dependent Claim
31 words
A process for electrochemically treating ores as claimed in claim 1 wherein an a.c. voltage is applied to the electrodes to cause each electrode surface to alternately become cathodic and anodic.
Claim 11
Dependent Claim
46 words
A process for electrochemically treating ores as claimed in claim 1 wherein an a.c. voltage is first applied to the electrodes for dissolution of the precious metals, and thereafter a d.c. voltage is applied to the electrodes and the precious metals are recovered at the cathode.
Claim 12
Dependent Claim
27 words
A process for electrochemically treating ores as claimed in claim 1 further comprising maintaining the alkalinity of the slurry at at least about 0.01 equivalents per liter.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-02-12 | 1982-08-14 | 1983-02-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-02-12 | 1986-08-14 | 1987-02-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-02-12 | 1990-08-14 | 1991-02-13 | $7700.00 | Window Closed / Lapsed |