Jet flow device for injecting gas into molten metal and process

• US 5,340,379 A
• Filed: 04/09/1993
• Issued: 08/23/1994
• Est. Priority Date: 11/09/1990
• Status: Expired due to Fees

• Current Assignee: Alcan Incorporated (Rio Tinto Limited)
• Original Assignee: Alcan Incorporated (Rio Tinto Limited)
• Inventors: Dube, Ghyslain, Tremblay, Francois
• Primary Examiner(s): Andrews, Melvyn J.
• Application Number:
  US08/039,099
• Time in Patent Office: 501 Days
• Field of Search: 266/216, 266/233, 266/208, 266/218, 75/708, 75/680, 75/681
• US Class Current: 75/680
• CPC Class Codes: B01F 23/23 by introducing gases into liquid media, e.g. for producing aerated liquids
• CPC Class Codes: B01F 23/23121 having injection means, e.g. nozzles with circumferential outlet
• CPC Class Codes: B01F 23/454 by injecting a mixture of liquid and gas
• CPC Class Codes: B01F 25/312 with Venturi elements; Details thereof
• CPC Class Codes: C22B 21/0084 melting and handling molten aluminium C22B21/02, C22B21/04 and C22B21/06 take precedence
• CPC Class Codes: C22B 21/064 using inert or reactive gases C22B21/066 and C22B21/068 take precedence
• CPC Class Codes: C22B 9/02 Refining by liquating, filtering, centrifuging, distilling, or supersonic wave action including acoustic waves; C22B9/003, C22B9/006, C22B9/05, C22B9/22 take precedence
• CPC Class Codes: C22B 9/05 Refining by treating with gases, e.g. gas flushing also refining by means of a material generating gas in situ
• CPC Class Codes: F27D 3/16 Introducing a fluid jet or current into the charge porous elements for gas flushing of molten metals B22D1/005
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

A device is described for injecting gas into molten metal, e.g. molten aluminum, in a furnace chamber. It comprises: (a) a stirring apparatus having a reservoir chamber separate from the furnace chamber, a connector portion with an orifice connecting the interior of the furnace and the reservoir for the passage of the molten metal between them through the connector portion, vacuum/pressure generating means connected to the reservoir chamber interior for alternatively and successively producing therein a vacuum for drawing molten metal into its interior from the furnace chamber and a positive pressure for expelling the molten metal therefrom into the furnace chamber through the orifice in the form of a high velocity stirring jet, and (b) gas injector means adapted to inject gas into the high velocity stirring jet such that the gas is broken down into a large number of small bubbles which are circulated throughout the furnace chamber with the stirring jet.

Claims

1. A device for injecting gas into molten metal in a furnace chamber comprising:

(a) a stirring apparatus having a reservoir chamber separate from the furnace chamber, a connector portion with an orifice connecting the interior of the furnace and the reservoir for the passage of the molten metal between them through the connector portion, vacuum/pressure generating means connected to the reservoir chamber interior for alternatively and successively producing therein a vacuum for drawing molten metal into its interior from the furnace chamber and a positive pressure for expelling the molten metal therefrom into the furnace chamber through the orifice in the form of a high velocity stirring jet, and

(b) gas injector tube adapted to inject gas into the high velocity stirring jet emerging from the orifice in an axial core region thereof of maximum velocity such that the gas is broken down into a large number of small bubbles which are circulated throughout the furnace chamber with the stirring jet.

2. A device according to claim 1 wherein the gas injector is a tube extending into the furnace adjacent the orifice-containing connector portion and positioned with the outlet of the tube within a cone of maximum velocity of a metal jet emerging from said orifice-containing connector portion.

3. A device according to claim 2 wherein the tube outlet is positioned downstream from the orifice a distance equivalent to no more than five times the diameter of the orifice.

4. A device according to claim 3 wherein the orifice has a diameter of about 5-10 cm.

5. A device according to claim 4 wherein the stirrer reservoir has a capacity of 500-1000 kg.

6. A process for treating molten metal with a treatment gas comprising the steps of:

(a) providing a melt of a metal in a treatment device comprising a treatment vessel and a separate reservoir chamber flow connected to the treatment vessel by an orifice;

(b) heating the melt in the treatment vessel to maintain a desired treatment temperature,

(c) alternatively and successively producing in the reservoir chamber a vacuum for drawing molten metal into the reservoir from the treatment vessel and a positive pressure for expelling the molten metal therefrom through the orifice into the treatment vessel in the form of a high velocity jet and

(d) injecting a treatment gas through a tube into the high velocity jet emerging from the orifice in an axial core region thereof of maximum velocity such that the gas is broken down into a large number of small bubbles which are circulated throughout the treatment vessel with the jet.

7. A process according to claim 6 wherein the metal is aluminum.

8. A process according to claim 7 wherein the treatment gas is an inert gas.

9. A process according to claim 8 wherein the treatment gas includes a reactive component.

10. A process according to claim 9 wherein the reactive component is a chlorine and/or fluorine containing material.

11. A process according to claim 10 wherein the reactive component is chlorine.

12. A process according to claim 10 wherein the reactive component is SF₆ or SiF₄.

13. A process according to claim 6 wherein the metal jet emerges from the orifice at a speed of at least 1 m/sec.

14. A process according to claim 13 wherein the speed is 5.10 m/sec.

15. A process according to claim 13 wherein the treatment gas is injected directly into the jet emerging from the orifice at a distance downstream from the orifice equivalent to five times the diameter of the orifice.

16. A process according to claim 13 wherein the treatment gas is injected directly into an axial cone of maximum velocity in the jet emerging from the orifice.

17. A process according to claim 6 wherein each suction cycle has a duration of about 10-15 seconds and each jet discharge cycle has a duration of about 10-15 seconds.