Cyanide removal from aqueous streams

• US 4,537,686 A
• Filed: 03/08/1984
• Issued: 08/27/1985
• Est. Priority Date: 01/28/1981
• Status: Expired due to Term

• Current Assignee: INCO Limited A Company Canada
• Original Assignee: Inco Limited (Caixa de Previdência Dos Funcionários Do Banco Do Brasil)
• Inventors: Devuyst, Eric A., Ettel, Victor A., Schitka, Konstantin J., Borbely, Gyula J., Mosoiu, Marcel A.
• Primary Examiner(s): Wyse, Thomas
• Application Number:
  US06/587,611
• Time in Patent Office: 537 Days
• Field of Search: 210/761-763, 210/904, 210/721, 210/712, 210/719, 210/724, 210/726, 210/757, 210/912, 210/713
• US Class Current: 210/713
• CPC Class Codes: C02F 1/725 by catalytic oxidation
• CPC Class Codes: C02F 2101/18 Cyanides
• CPC Class Codes: Y10S 210/904 -CN containing

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.

Claims

1. 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.

2. The method in accordance with claim 1 wherein said solution is treated in continuous fashion in one or more stages.

3. The method in accordance with claim 1 wherein the pH is about 5 to about 10.

4. 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.

5. The method in accordance with claim 1 wherein pH control is effected by an alkali or alkaline earth metal base.

6. The method in accordance with claim 1 wherein the pH is below 6.5 and the base is limestone.

7. 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.

8. 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.

9. The method in accordance with claim 1 wherein the ratio of copper to total cyanide is at least about 0.25 gm/gm.

10. The method in accordance with claim 1 wherein said effluent solution contains up to 1000 ppm of total cyanide.

11. The method in accordance with claim 1 wherein sulfur dioxide and air are employed in admixture.

12. The method in accordance with claim 8 wherein said sulfur dioxide and air are introduced with agitation.

13. 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.

14. The method in accordance with claim 13 wherein said effluent solution is quiescent during said oxygen introduction.

15. 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.

16. 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.

17. 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.

18. 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.

19. 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.

20. 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.

21. 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.