IP Library Granted Patent US 9,803,260
Granted Patent B2
US 9,803,260 · App. 14/782,356 · Granted Oct 31, 2017

Use of cationic surfactants in the cyanidation of refractory carbonaceous ores for recovery of metals

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Quick Facts
Patent No.
US 9,803,260
App. No.
14/782,356
Granted
Oct 31, 2017
Kind
B2
Abstract

A process for recovery of precious metals from ores or concentrates containing refractory carbonaceous material by cyanidation leaching. The process involves addition to the ores or concentrates at least one cationic surfactant before or during the addition of cyanide-containing solution. The agent enables the recovery of precious metals by cyanidation from high preg-robbing carbonaceous ores and improves the recovery of precious metals by cyanidation from medium to low preg-robbing carbonaceous ores. The agent also prevents froth and foaming formation during the cyanidation process.

Claims (24)

1. A method for recovering a metal from ore or concentrate containing carbonaceous material by cyanidation leaching, the method comprising the following steps:

a) treating the ore or concentrate containing carbonaceous material with at least one cationic surfactant in order to reduce or prevent retention of said metal or a cyanide complex of said metal by said ore or concentrate as a result of the presence of said carbonaceous material in said ore or concentrate, the ore or concentrate after said treating being designated “treated ore or concentrate”, and

b) cyanidation leaching of the treated ore or concentrate,

wherein the cationic surfactant is a saturated or unsaturated alkyl amine or derivative thereof,

wherein the alkyl amine is selected from the group consisting of primary alkyl amines, secondary alkyl amines, tertiary alkyl amines and alkyl polyamines, and

wherein the alkyl amine has an alkyl chain length of 14 to 40.

2. The method of claim 1 , further comprising a step of adding a cyanide-containing solution to the ore or concentrate.

3. The method of claim 1 , further comprising a step of roasting the ore or concentrate prior to the treating step.

4. The method of claim 1 , wherein the ore or concentrate is in an aqueous ore slurry with particle size 80% passing 30 mesh or finer and a pulp density of 5% to 80%.

5. The method of claim 1 , further comprising a step of oxidizing the ore or concentrate prior to the treating step.

6. The method of claim 1 , wherein the alkyl amine is animal based or vegetable based fatty alkyl amine.

7. The method of claim 1 , wherein the alkyl amine is alkoxylated.

8. The method of claim 1 , wherein the cationic surfactant is selected from the group consisting of a salt of the alkyl amine, an alkyl amine derivative, and combinations thereof.

9. The method of claim 1 , wherein the cationic surfactant is an alkyl quaternary ammonium salt.

10. The method of claim 1 , wherein the cationic surfactant is an alkyl amine oxide.

11. The method of claim 1 , wherein the cationic surfactant is selected from the group consisting of an alkyl amide, amidoamine, imidazoline, and combinations thereof.

12. The method of claim 1 , wherein the ore or concentrate is treated with the cationic surfactant and at least one other surfactant selected from the group consisting of a cationic surfactant different from the cationic surfactant, an anionic surfactant, a non-ionic surfactant, an amphoteric surfactant, and combinations thereof.

13. The method of claim 1 , further comprising a step of adding a defoamer to the ore or concentrate prior to the step of cyanidation leaching.

14. A method for recovering a metal from ore or concentrate containing carbonaceous material by cyanidation leaching, the method comprising the following steps:

a) treating the ore or concentrate containing carbonaceous material with at least one cationic surfactant in order to reduce or prevent retention of said metal or a cyanide complex of said metal by said ore or concentrate as a result of the presence of said carbonaceous material in said ore or concentrate, the ore or concentrate after said treating being designated “treated ore or concentrate”, and

b) cyanidation leaching of the treated ore or concentrate,

wherein the cationic surfactant is a saturated or unsaturated alkyl amine or derivative thereof,

wherein the alkyl amine is selected from the group consisting of primary alkyl amines, secondary alkyl amines, and tertiary alkyl amines, and

wherein the alkyl amine has an alkyl chain length of 14 to 40.

Assignments (3)
SECURITY INTEREST Recorded Oct 1, 2018
From: STARFRUIT US MERGER SUB 1 LLC; STARFRUIT US MERGER SUB 2 LLC; AKZO NOBEL SURFACE CHEMISTRY LLC; AKZO NOBEL CHEMICALS B.V.; AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
To: WILMINGTON TRUST (LONDON) LIMITED, AS COLLATERAL AGENT
Reel/Frame 047231/0001 →
CHANGE OF ADDRESS Recorded Jul 12, 2017
From: AKZO NOBEL CHEMICAL INTERNATIONAL B.V.
To: AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
Reel/Frame 043164/0083 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 21, 2016
From: ZHOU, QIONG; JIANG, JUNHUA; CHOI, YEONUK
To: AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
Reel/Frame 037543/0403 →