Methods and systems for controlling impurity metal concentration during metallurgic processes

Patent metadata

Field	Value
Publication number	US-10060040-B2
Application number	US-201514640245-A
Country	US
Kind code	B2
Filing date	Mar 6, 2015
Priority date	Mar 7, 2014
Publication date	Aug 28, 2018
Grant date	Aug 28, 2018

Abstract

Reagent compositions, methods and systems for reducing concentrations of impurity metals during metallurgic processes. Certain methods and systems in particular pertain to control of iron concentration in copper electrowinning electrolyte solutions.

First claim

What is claimed is:

1. A method of controlling an iron concentration in a copper extraction system, wherein the copper extraction system comprises a copper electrowinning station, the method comprising:
a. introducing a copper rich electrolyte into the copper electrowinning station and removing a copper lean electrolyte from the copper electrowinning station;
b. determining an iron transfer to the copper electrowinning station;
c. removing a bleed portion of the electrolyte solution from the copper electrowinning station at a bleed stream rate, and introducing the bleed portion into a solution comprising an organic solvent and an iron extraction agent, wherein the iron extraction agent is a monoalkyl phosphate ester having a structure represented by:
where R 1 comprises a linear, branched or cyclic alkyl or aryl group, and R 2 and R 3 are each H, and
wherein contacting the bleed portion with the solution provides an iron-loaded organic;
d. determining an iron removal of the iron extraction stage, wherein the bleed stream rate is proportional to the ratio of the iron transfer and the iron removal;
e. stripping the iron from the iron-loaded organic into an iron-rich strip solution; and
f. leaching copper ore with the iron-rich strip solution.

2. The method of claim 1 , wherein determining the iron transfer comprises measuring difference in iron concentration entering and exiting the copper electrowinning station.

3. The method of claim 1 , wherein the copper extraction system further comprises an extraction stage in which copper is extracted into an organic phase to provide a loaded organic, and a strip stage in which copper is stripped from the organic phase to provide a stripped organic, and determining the iron transfer comprises calculating the sum of: a. an iron strip rate determined by the difference in iron concentration between the loaded organic and the stripped organic; and b. an iron entrainment rate determined by an iron concentration in an aqueous entrainment in the organic phase.

4. The method of claim 1 , wherein the iron transfer is an iron amount per unit of time, an iron amount, an iron concentration or an iron concentration per unit of time.

5. The method of claim 1 , wherein the iron removal is an iron amount per unit of time, an iron amount, an iron concentration or an iron concentration per unit of time.

6. The method of claim 1 , wherein R 1 is a branched or linear C 6 -C 12 alkyl group.

7. The method of claim 6 , wherein the monoalkyl phosphate ester comprises iso-octyl phosphoric acid, 2-ethylhexyl phosphoric acid, octophenyl phosphoric acid or nonylphenyl phosphoric acid.

8. The method of claim 1 , further comprising contacting the bleed portion with a modifier.

9. The method of claim 8 , wherein the modifier comprises a C 8 -C 16 linear, branched or cyclic or aryl alcohol.

10. The method of claim 1 , wherein the extraction agent further comprises a dialkyl phosphate ester.

Assignees

• Basf Se

Inventors

• Bender Jack
• Emmerich Nathan C

Classifications

• C25C7/04

  Diaphragms; Spacing elements · CPC title

• C22B3/02

  Apparatus therefor · CPC title

• C25C1/12 Primary

  of copper · CPC title

• C22B15/0065

  Leaching or slurrying (with organic compounds C22B3/16) · CPC title

• C25C7/06

  Operating or servicing · CPC title