Flotation line and a method

Patent metadata

Field	Value
Publication number	US-11554379-B2
Application number	US-201716321736-A
Country	US
Kind code	B2
Filing date	Jul 28, 2017
Priority date	Aug 5, 2016
Publication date	Jan 17, 2023
Grant date	Jan 17, 2023

Abstract

A flotation line for treating mineral ore particles suspended in slurry, including at least three flotation units arranged in fluid connection with each other for allowing gravity-driven slurry flow between flotation units, and a feed inlet for supplying slurry into a first flotation unit; wherein at least three flotation units are configured to be uniplanar, each flotation unit includes at least one flotation cell; and wherein the launder lip height of each uniplanar flotation unit is lower than the launder lip height of the preceding uniplanar flotation unit in the direction of the slurry flow, so that an angle of sloping between a first uniplanar flotation cell, equipped with a launder lip and being larger than 150 m3, and a last uniplanar flotation cell, equipped with a launder lip and being larger than 40 m3, is formed; and the angle is 1.5 to 10 degrees relative to horizontal.

First claim

The invention claimed is:

1. A flotation line for treating mineral ore particles suspended in slurry, the flotation line comprising:
at least three flotation units arranged in fluid connection with each other for allowing gravity-driven slurry flow between the at least three flotation units, each flotation unit of the at least three flotation units including at least one flotation cell, so that each flotation unit includes at least one flotation cell equipped with a launder lip, at least one flotation cell equipped with a mixing apparatus, and at least one flotation cell equipped with a dispersed gas feeding mechanism; and
a feed inlet for supplying slurry into a first flotation unit of the at least three flotation units, wherein:
the at least three flotation units are configured to be uniplanar, so that bottoms of the at least three flotation units are positioned at least partially within a vertical range measured from a level of a bottom of a first flotation cell equipped with a launder lip and being larger than 150 m 3 , wherein the vertical range is defined as a distance between a first line drawn at an angle of +1° relative to horizontal and a second line drawn at an angle of −0.1° relative to horizontal, the first and second lines starting from a lowest functional position of the bottom of the first flotation cell;
each flotation cell equipped with a launder lip comprises a slurry inlet, a tailings outlet, and a concentrate outlet;
a flotation unit launder lip height of each uniplanar flotation unit is lower than a flotation unit launder lip height of a preceding uniplanar flotation unit in a direction of a slurry flow, the flotation unit launder lip height determined by the launder lip of a flotation cell of a respective flotation unit, measured from a same position for each flotation unit of the flotation line, so that an angle of sloping between a horizontal line drawn through a launder lip height of a first uniplanar flotation cell and a line drawn from a point of a first uniplanar flotation cell, equipped with a launder lip and being larger than 150 m 3 , and a corresponding point of a last uniplanar flotation cell, equipped with a launder lip and being larger than 40 m 3 , is formed; and
the angle of sloping is 1.5 to 10 degrees relative to horizontal, the angle being calculated via corresponding positions of launder lip heights of the first uniplanar flotation cell and the last uniplanar flotation cell.

2. The flotation line according to claim 1 , wherein the angle of sloping is 2 to 6 degrees.

3. The flotation line according to claim 1 , wherein the angle of sloping is calculated from a center of a launder lip plane of said flotation cells.

4. The flotation line according to claim 1 , wherein at least 80% of a volume of uniplanar flotation cells comprising a mixing apparatus is configured to be mixed by a mechanical agitator.

5. The flotation line according to claim 1 , wherein a given uniplanar flotation cell is equipped with a launder lip, a mixing apparatus, and a dispersed gas feeding mechanism.

6. The flotation line according to claim 1 , wherein the tailings outlet of a uniplanar flotation cell equipped with a launder lip is connected to a slurry inlet of a subsequent uniplanar flotation cell equipped with a mixing apparatus.

7. The flotation line according to claim 1 , wherein the flotation unit launder lip height of each uniplanar flotation unit is at least 400 mm lower than the flotation unit launder lip height of the preceding uniplanar flotation unit.

8. The flotation line according to claim 1 , wherein flotation cells that comprise at least 80% of a uniplanar flotation cell volume have a launder lip height-to-cell diameter ratio of less than 1.2.

9. The flotation line according to claim 1 , wherein flotation cells that comprise at least 80% of a uniplanar flotation cell volume have a launder lip height-to-cell diameter ratio of less than 1.0.

10. The flotation line according to claim 1 , wherein flotation cells that comprise at least 80% of a uniplanar flotation cell volume have a launder lip height-to-cell diameter ratio of less than 0.4 to 0.9.

11. The flotation line according to claim 1 , wherein the uniplanar flotation cells that comprise a launder lip and are larger than 150 m 3 , have a launder lip height-to-cell diameter ratio of less than 1.2.

12. The flotation line according to claim 1 , wherein the uniplanar flotation cells that comprise a launder lip and are larger than 150 m 3 have a launder lip height-to-cell diameter ratio of less than 1.0.

13. The flotation line according to claim 1 , wherein the uniplanar flotation cells that comprise a launder lip and are larger than 150 m 3 have a launder lip height-to-cell diameter ratio of less than 0.4 to 0.9.

14. The flotation line according to claim 1 , wherein a size of at least one uniplanar flotation cell equipped with a launder lip is at least 400 m 3 .

15. The flotation line according to claim 1 , wherein a size of the first uniplanar flotation cell, equipped with a launder lip, is at least 400 m 3 .

16. The flotation line according to claim 1 , wherein the at least one flotation cell of a second uniplanar flotation unit in the direction of the slurry flow is smaller than the at least one flotation cell of the first uniplanar flotation unit.

17. The flotation line according to claim 1 , wherein the at least one flotation cell of a second uniplanar flotation unit is at least 10% smaller than the at least one flotation cell of the first uniplanar flotation unit.

18. The flotation line according to claim 1 , wherein the at least one flotation cell of a third uniplanar flotation unit in the direction of the slurry flow is at least 30% smaller than the at least one flotation cell of the first uniplanar flotation unit.

19. The flotation line according to claim 1 , wherein the launder lip height of the first flotation cell, equipped with a launder lip, is at least 6 m.

20. The flotation line according to claim 1 , wherein a fluid connection is a direct connection between an outlet of a preceding uniplanar flotation unit and an inlet of a subsequent uniplanar flotation unit in the direction of the slurry flow.

21. The flotation line according to claim 1 , wherein fluid connections between uniplanar flotation units larger than 40 m 3 are uniplanar.

22. The flotation line according to claim 1 , wherein the at least one flotation cell in a uniplanar flotation unit is a froth flotation cell.

23. The flotation line according to claim 1 , wherein the flotation line comprises three to ten uniplanar flotation units larger than 40 m 3 .

24. The flotation line according to claim 1 , wherein the flotation line comprises four to seven uniplanar flotation units larger than 40 m 3 .

25. The flotation line according to claim 1 , wherein the flotation line comprises three to ten uniplanar flotation cells larger than 40 m 3 .

26. The flotation line according to claim 1 , wherein the flotation line comprises four to seven uniplanar flotation cells larger than 40 m 3 .

27. The flotation line according to claim 1 , wherein at least 80% of the uniplanar flotation cells have a diameter of at least 3.5 m.

28. The flotation line according to claim 1 , wherein at least 80% of the uniplanar flotation cells have a diameter of at least 6 m.

29. The flotation line according to claim 1 , where

Assignees

• Outotec Finland Oy

Inventors

• Bourke Peter Gerard
• Rinne Antti
• Coleman Rob

Classifications

• B03D1/1456

  Feed mechanisms for the slurry · CPC title

• B03D1/1443

  Feed or discharge mechanisms for flotation tanks · CPC title

• B03D1/02 Primary

  Froth-flotation processes · CPC title

• B03D1/1406

  with special arrangement of a plurality of flotation cells, e.g. positioning a flotation cell inside another · CPC title

• B03D1/1462

  Discharge mechanisms for the froth · CPC title