Fire refining of blister copper

Patent metadata

Field	Value
Publication number	US-10648060-B2
Application number	US-201615570831-A
Country	US
Kind code	B2
Filing date	May 3, 2016
Priority date	May 6, 2015
Publication date	May 12, 2020
Grant date	May 12, 2020

Abstract

Provided herein is a process of fire refining blister copper, comprising the steps of (a) providing molten blister copper into an anode furnace; (b) when sulfur concentration of the molten blister copper provided in step (a) is above a first prescribed target value, oxidizing sulfur in the molten blister copper by blowing oxygen containing gas into the molten blister copper until the first prescribed target value has been reached; (c) subsequently lowering the sulfur and oxygen content in blister copper by blowing inert gas into the molten blister copper until a second prescribed target value has been reached, wherein the inert phase (c) is continued until the second prescribed target value of the oxygen concentration is below 4000 ppm, and the second prescribed target value of the sulfur concentration is below 500 ppm; (d) when certain condition(s) occur, subsequently reducing oxygen in the blister copper; and (e) optionally casting.

First claim

The invention claimed is:

1. A process of fire refining blister copper, comprising the steps of:
(a) providing molten blister copper into an anode furnace;
(b) oxidizing sulfur in the molten blister copper by blowing oxygen containing gas into the molten blister copper until a first prescribed target value has been reached;
(c) subsequently discontinuing blowing of the oxygen containing gas and lowering a sulfur and oxygen content in blister copper by blowing inert gas into the molten blister copper until a second prescribed target value has been reached, wherein an inert phase (c) is continued until the second prescribed target value of an oxygen concentration is below 4000 ppm, and the second prescribed target value of a sulfur concentration is below 500 ppm;
(d) subsequently discontinuing blowing of the inert gas and reducing oxygen in the blister copper by supplying a reducing agent into the molten blister copper until a third prescribed target value has been reached and anode copper is obtained; and
(e) optionally casting the obtained anode copper.

2. The process as claimed in claim 1 , wherein an oxidation phase (b) is continued until the first prescribed target value of the sulfur concentration in the blister copper is from 400 to 1000 ppm.

3. The process as claimed in claim 1 , wherein an oxidation phase (b) is continued until the first prescribed target value of the oxygen concentration in the molten blister copper is from 2000 to 5000 ppm.

4. The process as claimed in claim 1 , wherein the inert gas is nitrogen.

5. The process as claimed in claim 1 , wherein the inert phase (c) is continued until the second prescribed target value of the oxygen concentration is from 1500 to 2500 ppm.

6. The process as claimed in claim 1 , wherein the inert phase (c) is continued until the second prescribed target value of the sulfur concentration is below 200 ppm.

7. The process as claimed in claim 1 , wherein slag removal is performed at the end of an oxidation phase (b) and/or inert phase (c).

8. The process as claimed in claim 1 , wherein a reduction phase (d) is continued until the third prescribed target value of the oxygen concentration is below 3000 ppm.

9. The process as claimed in claim 1 , wherein a reduction phase (d) is continued until the third prescribed target value of the sulfur concentration is below 50 ppm.

10. The process as claimed in claim 1 , wherein the composition of blister copper is monitored during the fire refining and switching points between phases is determined by: measuring one or more of the parameters selected from the group consisting of sulfur and oxygen concentration from the blister copper, SO 2 concentration from the off-gas line, and optical monitoring of the off-gas composition; comparing measured value(s) of the parameter(s) with a predetermined reference value for the corresponding parameter; and when the predetermined reference value has been reached indicating that a next phase can be started and/or starting the next phase.

11. The process as claimed in claim 1 , wherein an oxidation phase (b) is continued until the first prescribed target value of the oxygen concentration in the molten blister copper is from 2100 to 3100 ppm.

12. The process as claimed in claim 1 , wherein the inert phase (c) is continued until the second prescribed target value of the oxygen concentration is from 2000 to 2300 ppm.

13. The process as claimed in claim 1 , wherein the inert phase (c) is continued until the second prescribed target value of the sulfur concentration is from 75 to 150 ppm.

14. The process as claimed in claim 1 , wherein slag removal is performed after the inert phase (c).

15. The process as claimed in claim 1 , wherein reduction phase (d) is continued until the third prescribed target value of the oxygen concentration is below 2300 ppm.

16. The process as claimed in claim 1 , wherein reduction phase (d) is continued until the third prescribed target value of the oxygen concentration is from 500 to 1500 ppm.

Assignees

• Outotec Finland Oy

Inventors

• Jaatinen Akusti
• Talvensaari Harri

Classifications

• C22B15/006 Primary

  working up of molten copper, e.g. refining · CPC title

• C22B9/05 Primary

  Refining by treating with gases, e.g. gas flushing {also refining by means of a material generating gas in situ} · CPC title

• C22B15/003

  Bath smelting or converting · CPC title

• C22B15/0028 Primary

  Smelting or converting · CPC title

• C22B15/0026

  Pyrometallurgy · CPC title