IP Library Granted Patent US 8,491,700
Granted Patent B2
US 8,491,700 · App. 13/724,860 · Granted Jul 23, 2013

Methods and systems for recovering rhenium from a copper leach

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Quick Facts
Patent No.
US 8,491,700
App. No.
13/724,860
Granted
Jul 23, 2013
Kind
B2
Abstract

Various embodiments provide new methods of rhenium recovery. The methods can include subjecting a metal-bearing solution to an activated carbon bed, and adsorbing rhenium onto the activated carbon. The methods can also include heating a basic aqueous elution solution and eluting the rhenium from the activated carbon with the heated elution solution. The methods can also incorporate an ion exchange as a rhenium recovery apparatus.

Claims (18)

1. A method for recovering rhenium, the method comprising:

feeding a metal-bearing leach solution comprising rhenium and copper over activated carbon to produce a remainder solution;

feeding said remainder solution into an ion exchange to produce an electrowinning solution;

recovering copper from the electrowinning solution; and

recovering rhenium from at least one of the activated carbon and the ion exchange.

2. The method according to claim 1 , wherein the recovering of rhenium from the activated carbon further comprises:

adsorbing said rhenium onto said activated carbon;

heating a basic aqueous solution to a temperature greater than about 105° C.; and

recovering said rhenium by eluting said rhenium from said activated carbon with said basic aqueous solution.

3. The method according to claim 2 , wherein said basic aqueous solution comprises a hydroxide salt.

4. The method according to claim 3 , wherein said hydroxide salt is at least one of sodium hydroxide, ammonium hydroxide, lithium hydroxide, and potassium hydroxide.

5. The method according to claim 3 , wherein said hydroxide salt is present in said basic aqueous solution in an amount from about 0.2% to about 5%.

6. The method according to claim 3 , wherein said hydroxide salt is sodium hydroxide in an amount from about 0.5% to about 2.5%.

7. The method according to claim 2 , wherein said rhenium eluted from said activated carbon is greater than about 95% of rhenium in said metal-bearing leach solution.

8. The method according to claim 2 , wherein the basic aqueous solution is heated to a temperature from about 105° C. to about 115° C.

9. The method according to claim 2 , wherein the basic aqueous solution is heated to a temperature from about 108° C. to about 110° C.

10. The method according to claim 1 , further comprising leaching a metal-bearing material to yield said metal-bearing each solution.

11. The method according to claim 1 , wherein said leach solution comprises less than 1 mg/L rhenium.

Assignments (3)
CHANGE OF NAME Recorded Jul 23, 2014
From: FREEPORT-MCMORAN CORPORATION
To: FREEPORT MINERALS CORPORATION
Reel/Frame 033389/0300 →
MERGER Recorded Jul 17, 2014
From: FREEPORT-MCMORAN CORPORATION
To: FREEPORT-MCMORAN CORPORATION
Reel/Frame 033357/0849 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 8, 2013
From: WATERMAN, BRETT T; DIXON, STEVE NELS; MORELLI, THERESA LINNE; OWUSU, GEORGE; ORMSBY, STEFKA TODOROVA
To: FREEPORT-MCMORAN CORPORATION
Reel/Frame 029953/0472 →