US4397689A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the extraction of precious metals from concentrates thereof
Assignee: Vale Canada Ltd
•
Filing: 1981-09-01
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Granted: 1983-08-09
•
Expires: 2001-09-01
Abstract
Abstract The process comprises the steps of leaching the concentrate with hot hydrochloric acid and chlorine gas to dissolve most of the gold, platinum and palladium, treating the residue from the leaching step with an excess of an alkaline oxidizing agent to solubilize the ruthenium, slurrying the resulting solids in water, combining the precious metal values from the slurry with the liquor from the leaching step and releaching the resulting slurry with hot hydrochloric acid and chlorine. The leach liquor which is then separated from the remaining solids is a chloride solution which contains substantially all the platinum group metals and gold present in the concentrate.
Inventors
- 👤 Richard K. Lea
- 👤 Julian D. Edwards
- 👤 D. Frederick Colton
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 13:51
CPC Classifications
C; C01; C01G; C01G7/00; C01G7/003; C01G55/00; C01G55/001; C22; C22B; C22B11/00; C22B11/04; C22B3/00; C22B3/20; C22B3/26; C22B3/262; C22B3/302; C22B3/306; C22B3/32; C22B3/34; C22B3/38; C22B3/384; C22B3/3846; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
160 words
A process for leaching a concentrate containing precious metals, comprising the steps of leaching the concentrate with hydrochloric acid and chlorine at a temperature in the range from 60° to 105° C. to dissolve most of the gold, platinum and palladium present leaving a solid residue containing substantially all the other precious metals, separating and recovering silver from the process if the silver content of the concentrate is greater than about 10% (by weight) of the concentrate, separating the residue and treating it with an excess (on a weight for weight basis) of sodium peroxide at a temperature in the range from 550° to 650° C. to solubilise the ruthenium, slurrying the resulting solids in water, combining the precious metal values from the slurry with the liquor from the leaching step, releaching the resulting slurry with hydrochloric acid and chlorine at a temperature in the range from 60° to 105° C. and separating the leach liquor from the remaining solids.
Claim 2
Dependent Claim
160 words
A process for leaching a concentrate containing precious metals, comprising the steps of leaching the concentrate with hydrochloric acid and chlorine at a temperature in the range from 60° to 105° C. to dissolve most of the gold, platinum and palladium present leaving a solid residue containing substantially all the other precious metals, separating and recovering silver from the process if the silver content of the concentrate is greater than about 10% (by weight) of the concentrate, separating the residue and treating it with an excess (on a weight for weight basis) of sodium peroxide at a temperature in the range from 550° to 650° C. to solubilise the ruthenium, slurrying the resulting solids in water, combining the precious metal values from the slurry with the liquor from the leaching step, releaching the resulting slurry with hydrochloric acid and chlorine at a temperature in the range from 60° to 105° C. and separating the leach liquor from the remaining solids.
Claim 3
Dependent Claim
32 words
A process as claimed in clam 1 wherein the precious metal values from the slurry are combined with the liquor from the leaching step by combining the whole slurry with the liquor.
Claim 4
Dependent Claim
57 words
A process as claimed in claim 1 wherein the precious metal values from the slurry are combined with the liquor from the leaching step by reducing the ruthenium in the slurry liquor to ruthenium metal which precipitates with the slurry solids, filtering the slurry and combining the solids thus obtained with the liquor from the leaching step.
Claim 5
Dependent Claim
15 words
A process as claimed in claim 3, wherein the ruthenium is reduced using formic acid.
Claim 6
Dependent Claim
35 words
A process as claimed in claim 1 which further includes the step of leaching the concentrate with nitric acid to dissolve some of the silver prior to leaching the concentrate with hydrochloric acid and chlorine.
Claim 7
Dependent Claim
40 words
A process as claimed in claim 1 which further includes the step of treating the solid residue from the leaching step with aqueous sodium hydroxide and then with nitric acid to remove silver from the residue prior to oxidation thereof.
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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) | 1986-08-08 | 1987-02-07 | 1987-08-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-08-08 | 1991-02-07 | 1991-08-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-08-08 | 1995-02-07 | 1995-08-09 | $7700.00 | Window Closed / Lapsed |