US4149880A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Recovery of copper from arsenic containing metallurgical waste materials
Assignee: Kennecott Utah Copper LLC
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Filing: 1978-07-19
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Granted: 1979-04-17
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Expires: 1998-07-19
Abstract
Abstract Highly toxic metallurgical waste materials from copper smelting and/or refining operations are processed on a cyclic basis for recovering copper values therefrom while protecting the environment from contamination. The waste materials, usually smelter flue dust and/or refinery sludge containing copper values and principally arsenic, bismuth, lead, antimony, and cadmium, as toxic values, with or without added sulfuric acid, are reacted in an autoclave at an overpressure atmosphere of O2. The resulting solution, pregnant with copper and still containing a significant amount of arsenic, i.e. from about 0.5 to about 2.0 grams per liter, is subjected to copper cementation on metallic iron to recover copper and to provide iron values in the solution while substantially eliminating residual toxic constituents, surprisingly without the evolution of arsine gas. The copper-barren but iron-containing solution is then recycled to the leaching step. The cement copper precipitate is smelted along with copper ore concentrates, while the solid residue from the leaching step is discharged to a tailings pond or the like as an environmentally safe, insoluble residue.
Inventors
- 👤 John D. Prater
- 👤 Barry A. Wells
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 12:47
CPC Classifications
C; C22; C22B; C22B15/00; C22B15/0063; C22B15/0084; C22B15/0089; C22B15/0091; C22B15/0065; C22B15/0067; C22B15/0071; C22B7/00; C22B7/006; C22B7/007; C22B7/02; Y; Y02; Y02P; Y02P10/00; Y02P10/20
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
174 words
In a process for the recovery of copper values from highly toxic, smelter flue dusts and/or refinery sludges containing arsenic values as at least part of the toxic constituents, which process includes the leaching of such a flue dust and/or sludge with sulfuric acid at elevated temperature and under a pressurized oxygen atmosphere for solubilizing copper values and rendering insoluble the highly toxic values, the improvement comprising conducting the leaching step under such conditions of sulfuric acid concentration, temperature, and pressure as will precipitate toxic constituents while leaving a relatively small but significant amount of arsenic solubilized in the resulting copper-pregnant leach solution; separating the liquid and solid phases from the leaching step; recovering copper values from the pregnant leach solution by cementation on metallic iron, there being substantially no evolution of arsine gas during the cementation step of the process; separating the solid and liquid phases of the copper cementation step; and recycling the barren leach solution from the cementation step to the aforesaid leaching step to supply solubilized iron values during leaching.
Claim 2
Dependent Claim
174 words
In a process for the recovery of copper values from highly toxic, smelter flue dusts and/or refinery sludges containing arsenic values as at least part of the toxic constituents, which process includes the leaching of such a flue dust and/or sludge with sulfuric acid at elevated temperature and under a pressurized oxygen atmosphere for solubilizing copper values and rendering insoluble the highly toxic values, the improvement comprising conducting the leaching step under such conditions of sulfuric acid concentration, temperature, and pressure as will precipitate toxic constituents while leaving a relatively small but significant amount of arsenic solubilized in the resulting copper-pregnant leach solution; separating the liquid and solid phases from the leaching step; recovering copper values from the pregnant leach solution by cementation on metallic iron, there being substantially no evolution of arsine gas during the cementation step of the process; separating the solid and liquid phases of the copper cementation step; and recycling the barren leach solution from the cementation step to the aforesaid leaching step to supply solubilized iron values during leaching.
Claim 3
Dependent Claim
34 words
The improvement of claim 1, wherein the solids are recycled to the smelter; and a major portion of the barren leach solution is used to slurry the feed materials prior to the leaching step.
Claim 4
Dependent Claim
41 words
The improvement of claim 2, wherein the leached material also contains zinc values and a minor portion of the barren leach solution is treated for the recovery of the zinc values, the residual liquid not being returned to the processing circuit.
Claim 5
Dependent Claim
32 words
The improvement of claim 1, wherein the leached material also contains molybdenum values and the pregnant leach solution is treated for the recovery of molybdenum values prior to the copper cementation step.
Claim 6
Dependent Claim
27 words
The improvement of claim 1, wherein the leached material also contains one or more additional toxic values from the group consisting of bismuth, lead, antimony, and cadmium.
Claim 7
Dependent Claim
32 words
The improvement of claim 1, wherein the relatively small but significant amount of arsenic left in the copper-pregnant leach solution is within the range of about 0.5 to 2.0 grams per liter.
Claim 8
Dependent Claim
28 words
The improvement of claim 6, wherein the feed material contains about 13.5% copper and about 13.5% arsenic, and the sulfuric acid concentration is about 44 grams per liter.
Claim 9
Dependent Claim
30 words
The improvement of claim 1, wherein the relatively small but significant amount of arsenic left in the copper-pregnant leach solution is within the range of about 1.0 gram per liter.
Claim 10
Dependent Claim
67 words
The improvement of claim 1, wherein the feed material contains about 13.5% copper and about 13.5% arsenic, the relatively small but significant amount of arsenic left in the copper-pregnant leach solution is about 1.0 gram per liter, the sulfuric acid concentration is about 44 grams per liter, the temperature is about 140° Centigrade, the pressure is about 50 psi, and the leaching time is about one hour.
References Cited (Backward Citations)
US2686114A
Cited
US3330650A
Cited
US3455677A
Cited
US3880650A
Cited
US3902896A
Cited
US3929599A
Cited
US4026988A
Cited
US4071421A
Cited
US4076605A
Cited
US4071357A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-04-16 | 1982-10-16 | 1983-04-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-04-16 | 1986-10-16 | 1987-04-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-04-16 | 1990-10-16 | 1991-04-17 | $7700.00 | Window Closed / Lapsed |