Rotary injector and process of adding fluxing solids in molten aluminum

Patent metadata

Field	Value
Publication number	US-9840754-B2
Application number	US-201414894815-A
Country	US
Kind code	B2
Filing date	May 23, 2014
Priority date	May 29, 2013
Publication date	Dec 12, 2017
Grant date	Dec 12, 2017

Abstract

A rotary injector comprising an elongated shaft having a proximal end and a distal end, and an impeller at the distal end of the elongated shaft, the elongated shaft and the impeller being collectively rotatable during operation around an axis of the shaft, the rotary injector being hollow and having an internal supply conduit extending along the shaft and across the impeller, the supply conduit having an inlet at the proximal end of the shaft, a main portion extending from the inlet to a discharge portion, the discharge portion extending to an axial outlet, the discharge portion having a narrow end connecting the main portion of the supply conduit and a broader end at the axial outlet.

First claim

What is claimed is:

1. A process of treating molten aluminum using a rotary injector, the process comprising:
introducing a head of the rotary injector into the molten aluminum, the head of the rotary injector having an impeller with blades; and
while the head of the rotary injector, including the blades, is maintained immersed in the molten aluminum and rotated, simultaneously:
entraining particulate treatment solids using a carrier gas along a supply conduit along a shaft of the rotary injector and out from an axial outlet of the head of the rotary injector,
reducing a speed of the particulate treatment solids at a discharge portion of the supply conduit by an increase in a cross-sectional surface area of the supply conduit, and
shearing the particulate treatment solids exiting the axial outlet by rotation of the blades.

2. The process of claim 1 wherein the process is performed in a furnace having a quantity of aluminum of between 10 and 150 tons.

3. The process of claim 1 wherein the introducing the head of the rotary injector is performed when the molten aluminum is at a temperature below 720° C.

4. The process of claim 3 wherein the temperature is below 700° C.

5. The process of claim 3 wherein the entraining particulate treatment solids is performed during hot metal charging of the molten aluminum.

6. The process of claim 3 wherein the entraining particulate treatment solids is performed prior to a step of alloying.

7. The process of claim 3 wherein the entraining particulate treatment solids is performed in parallel with other furnace operations.

8. The process of claim 3 wherein the process is performed during charging a last potroom crucible, once a quantity of aluminum has reached 90 tons.

9. The process of claim 1 wherein the entraining particulate treatment solids is performed during hot metal charging of the molten aluminum.

10. The process of claim 1 wherein the entraining particulate treatment solids is performed prior to a step of alloying.

11. The process of claim 1 wherein the entraining particulate treatment solids is performed in parallel with other furnace operations.

12. The process of claim 1 wherein the process is performed during charging a last potroom crucible, once a quantity of aluminum has reached 90 tons.

13. A process of treating molten aluminum using a rotary injector, the process comprising:
introducing a head of the rotary injector into the molten aluminum;
while the head of the rotary injector is in the molten aluminum, entraining particulate treatment solids along a supply conduit along a shaft of the rotary injector and out from the head of the rotary injector, while rotating an impeller at the head of the rotary injector, and;
reducing a speed of the particulate treatment solids at a discharge portion of the supply conduit by an increase in a cross-sectional surface area of the supply conduit;
wherein the entraining the particulate treatment solids is performed during hot metal charging of the molten aluminum.

14. The process of claim 13 wherein the introducing the head of the rotary injector is performed when the molten aluminum is at a temperature below 720° C.

15. A process of treating molten aluminum using a rotary injector, the process comprising:
introducing a head of the rotary injector into the molten aluminum;
while the head of the rotary injector is in the molten aluminum, entraining particulate treatment solids along a supply conduit along a shaft of the rotary injector and out from the head of the rotary injector, while rotating an impeller at the head of the rotary injector, and;
reducing a speed of the particulate treatment solids at a discharge portion of the supply conduit by an increase in a cross-sectional surface area of the supply conduit;
wherein the process is performed during charging a last potroom crucible, once a quantity of aluminum has reached 90 tons.

16. The process of claim 15 wherein the introducing the head of the rotary injector is performed when the molten aluminum is at a temperature below 720° C.

17. A rotary injector comprising an elongated shaft having a proximal end and a distal end, and an impeller at the distal end of the elongated shaft, the elongated shaft and the impeller being collectively rotatable during operation around an axis of the shaft, the rotary injector being hollow and having an internal supply conduit extending along the shaft and through the impeller, the supply conduit having an inlet at the proximal end of the shaft, a main portion extending from the inlet to a discharge portion, the discharge portion extending to an axial outlet, the discharge portion having a narrow end connecting the main portion of the supply conduit and a broader end at the axial outlet; wherein the impeller has a distal face opposite the shaft, and blades protruding axially from the distal face, the blades being external to and surrounding the axial outlet.

18. The rotary injector of claim 1 wherein the discharge portion has a truncated conical shape.

19. The rotary injector of claim 18 wherein the axial outlet has a sharp edge.

20. The rotary injector of claim 1 wherein the axial outlet has a sharp edge.

21. The rotary injector of claim 1 wherein the discharge portion has an angle of between about 5 and 20° relative the shaft axis.

22. The rotary injector of claim 21 wherein the discharge portion has an angle of between 5 and 15° relative the shaft axis.

23. The rotary injector of claim 1 wherein the discharge portion has a length of about 3 inches along the shaft axis.

24. The rotary injector of claim 1 wherein a surface ratio of an upstream end of the discharge portion and the axial outlet is between 1.25 and 7.25.

25. The rotary injector of claim 1 wherein the impeller is provided in the form of a distinct component from the shaft and is removable therefrom.

26. The rotary injector of claim 25 wherein the distal end of the shaft and the impeller are matingly engaged to one another via corresponding male and female threads.

27. The rotary injector of claim 1 wherein the shaft and the impeller are made of graphite.

28. The rotary injector of claim 1 wherein when the rotary injector is used to treat molten metal, the axial outlet is directly exposed to the molten metal.

29. The rotary injector of claim 1 wherein the discharge portion and supply conduit are used to feed particulate treatment solids when the rotary injector is used to treat molten metal and are empty prior to said use.

30. The rotary injector of claim 1 wherein the distal face of the impeller is a radially-extending surface.

31. The rotary injector of claim 30 wherein the distal face of the impeller is oriented perpendicular to the axis of the shaft.

32. The rotary injector of claim 1 wherein the blades extend axially beyond the axial outlet of the supply conduit.

Assignees

• Rio Tinto Alcan Int Ltd

Inventors

• Langlais Joseph
• Waite Peter Donald
• Breton Francis
• Munger Serge

Classifications

• C22C21/00

  Alloys based on aluminium · CPC title

• C22B21/062 Primary

  using salt or fluxing agents (C22B21/064, C22B21/066, and C22B21/068 take precedence) · CPC title

• F27D3/0033

  charging of particulate material · CPC title

• C22C1/06

  with the use of special agents for refining or deoxidising · CPC title

• F27D27/00

  Stirring devices for molten material (charging or discharging liquid or molten material F27D3/14) · CPC title