Patent US4856857A successfully refreshed from Google Patents.
US4537686A
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Cyanide removal from aqueous streams
Assignee: Vale Canada Ltd
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Filing: 1984-03-08
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Granted: 1985-08-27
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Expires: 2004-03-08
Abstract
Abstract The cyanide content of waste waters containing the same is removed by treatment with sulfur dioxide or an alkali or alkaline earth metal sulfite or bisulfite in the presence of excess oxygen and a metal catalyst which is perferably copper.
Inventors
- 👤 Gyula J. Borbely
- 👤 Eric A. Devuyst
- 👤 Victor A. Ettel
- 👤 Marcel A. Mosoiu
- 👤 Konstantin J. Schitka
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 18:28
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/72; C02F1/725; C02F2101/00; C02F2101/10; C02F2101/16; C02F2101/18; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/903; Y10S210/904
Claims Analysis
Total Claims: 23
Claim 1
Independent Claim
62 words
The method for treating aqueous effluent to reduce the total cyanide content of said aqueous effluent solution which comprises treating said effluent solution with an oxygen-containing gas and a reagent from the group consisting of sulfur dioxide, an alkali or alkaline earth metal sulfite or bisulfite, at a pH of about 5 to about 12 in the presence of a copper catalyst.
Claim 2
Independent Claim
62 words
The method for treating aqueous effluent to reduce the total cyanide content of said aqueous effluent solution which comprises treating said effluent solution with an oxygen-containing gas and a reagent from the group consisting of sulfur dioxide, an alkali or alkaline earth metal sulfite or bisulfite, at a pH of about 5 to about 12 in the presence of a copper catalyst.
Claim 3
Dependent Claim
20 words
The method in accordance with claim 1 wherein said solution is treated in continuous fashion in one or more stages.
Claim 4
Dependent Claim
16 words
The method in accordance with claim 1 wherein the pH is about 5 to about 10.
Claim 5
Dependent Claim
67 words
The method in accordance with claim 1 wherein said solution also contains thiocyanate ion and the removal thereof by means of an oxygen-containing gas and a reagent from the group of sulfur dioxide and an alkali or alkaline earth sulfite or bisulfite subsequent to the essentially complete removal of cyanide ion is catalyzed by at least one metal from the group consisting of nickel, cobalt and manganese.
Claim 6
Dependent Claim
20 words
The method in accordance with claim 1 wherein pH control is effected by an alkali or alkaline earth metal base.
Claim 7
Dependent Claim
18 words
The method in accordance with claim 1 wherein the pH is below 6.5 and the base is limestone.
Claim 8
Dependent Claim
32 words
The method in accordance with claim 1 wherein treated solution containing copper in precipitated form is contacted with fresh solution containing cyanide species whereby said copper dissolves and catalyzes further impurity removal.
Claim 9
Dependent Claim
28 words
The method in accordance with claim 1 wherein a mixture of sulfur dioxide and air is employed which contains about 0.1 to about 6% sulfur dioxide, by volume.
Claim 10
Dependent Claim
21 words
The method in accordance with claim 1 wherein the ratio of copper to total cyanide is at least about 0.25 gm/gm.
Claim 11
Dependent Claim
19 words
The method in accordance with claim 1 wherein said effluent solution contains up to 1000 ppm of total cyanide.
Claim 12
Dependent Claim
16 words
The method in accordance with claim 1 wherein sulfur dioxide and air are employed in admixture.
Claim 13
Dependent Claim
17 words
The method in accordance with claim 8 wherein said sulfur dioxide and air are introduced with agitation.
Claim 14
Dependent Claim
38 words
The method in accordance with claim 1 wherein an agent from the group consisting of sulfur dioxide and alkali and alkaline earth metal sulfites and bisulfites is first introduced into said effluent solution and oxygen is thereafter introduced.
Claim 15
Dependent Claim
17 words
The method in accordance with claim 13 wherein said effluent solution is quiescent during said oxygen introduction.
Claim 16
Dependent Claim
47 words
The method in accordance with claim 1 wherein an agent from the group consisting of calcium sulfite, calcium bisulfite, and a combination of sulfur dioxide and lime is employed along with said oxygen-containing gas and the solution pH is maintained in the range of 5 to 7.
Claim 17
Dependent Claim
51 words
The method in accordance with claim 1 wherein the process is carried out at a pH in the range of 5 to about 8 and the pH is raised to about pH 10 after cyanide removal to hydrolyze metals contained in the effluent solution, thereby permitting metal recovery by solid-liquid separation.
Claim 18
Dependent Claim
27 words
The method in accordance with claim 1 wherein said aqueous effluent solution is the aqueous phase in a slurry containing solids derived from material subjected to cyanidation.
Claim 19
Dependent Claim
35 words
The method in accordance with claim 1 wherein said effluent solution is treated in stages, with recycle of precipitated solids containing catalyst metal to treat fresh solution whereby overall rate of cyanide removal is increased.
Claim 20
Independent Claim
120 words
The method for treating effluent solution and tailings from gold mining operations, said operations involving the leaching of comminuted gold ore with aqueous cyanide and recovery of soluble gold from said aqueous cyanide solution comprising treating essentially gold-barren aqueous effluent and tailings to reduce the total cyanide content thereof with an oxygen-containing gas and a reagent from the group consisting of sulfur dioxide and an alkaline earth or alkali metal sulfite or bisulfite at a pH of about 5 to about 12 in the presence of a copper catalyst at ambient temperature for said effluent and tailings and discharging said effluent and tailings to a disposal site without interposing any gold recovery operation between said treatment and said disposal site.
Claim 21
Independent Claim
120 words
The method for treating effluent solution and tailings from gold mining operations, said operations involving the leaching of comminuted gold ore with aqueous cyanide and recovery of soluble gold from said aqueous cyanide solution comprising treating essentially gold-barren aqueous effluent and tailings to reduce the total cyanide content thereof with an oxygen-containing gas and a reagent from the group consisting of sulfur dioxide and an alkaline earth or alkali metal sulfite or bisulfite at a pH of about 5 to about 12 in the presence of a copper catalyst at ambient temperature for said effluent and tailings and discharging said effluent and tailings to a disposal site without interposing any gold recovery operation between said treatment and said disposal site.
Claim 22
Dependent Claim
27 words
A method as in claim 19 wherein said effluent solution and tailings contain arsenic and said arsenic is removed from aqueous phase by treating with ferric ion.
Claim 23
Dependent Claim
26 words
A method as in claim 20 wherein said ferric ion is added after treatment to remove cyanide and at a pH of about 6 to 7.
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) | 1988-08-26 | 1989-02-25 | 1989-08-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-08-26 | 1993-02-25 | 1993-08-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-08-26 | 1997-02-25 | 1997-08-27 | $7700.00 | Window Closed / Lapsed |