Direct smelting process and apparatus

Patent metadata

Field	Value
Publication number	US-9175907-B2
Application number	US-201013148576-A
Country	US
Kind code	B2
Filing date	Feb 9, 2010
Priority date	Feb 9, 2009
Publication date	Nov 3, 2015
Grant date	Nov 3, 2015

Abstract

A process and apparatus for direct smelting metalliferous material is disclosed. The invention concentrates injection of solid feed materials comprising metalliferous material and carbonaceous material into a direct smelting vessel during the course of the process into a relatively small region within a metal layer in a molten bath in the vessel in order to generate a substantial upward movement of molten material and gas from the metal layer into a region in the vessel that is above the molten bath. In particular, the invention injects the solid feed materials with sufficient momentum and/or velocity via an opposed pair of lances that are oriented within the vessel and arranged to form overlapping plumes of injected material in the molten bath.

First claim

The invention claimed is:

1. A molten bath-based process for direct smelting metalliferous material and producing molten metal in a direct smelting vessel having a vessel floor and an upper region, which process comprises injecting a solid metalliferous material and a solid carbonaceous material through at least one pair of opposed injection lances extending downwardly and inwardly into a molten bath in the direct smelting vessel with longitudinal axes of the lances in the pair of opposed lances intersecting within a top three quarters of a metal layer in the molten bath, as measured from the vessel floor, and selecting momentum and/or velocity of the injected material to penetrate the molten bath and to coalesce in the molten bath below a nominal interface of molten metal and molten slag in the molten bath under quiescent conditions, whereby plumes of injected material from the lances overlap in a central region of a metal layer in the molten bath and the metalliferous material at least substantially melts in the metal layer and there is upward movement of molten material and gas from the central region of the metal layer.

2. The process defined in claim 1 wherein the longitudinal axes of the lances intersect above the vessel floor.

3. The process defined in claim 1 wherein the metalliferous material and the carbonaceous material are pneumatically injected into the smelting vessel whereby the material is entrained in a carrier gas.

4. The process defined in claim 1 , wherein the process melts at least 75% by weight of the metalliferous material injected via the lances before this material passes into a slag region of the molten bath.

5. The process defined in claim 1 comprising supplying at least 75% by weight of the metalliferous material and the carbonaceous material that is supplied to the direct smelting vessel during the process via the lances.

6. The process defined in claim 1 comprising operating in a range of pressures between 0.5 barg and 1.2 barg.

7. The process defined in claim 1 comprising injecting the metalliferous material and the carbonaceous material from the lances towards a vertical centreline of the direct smelting vessel.

8. The process defined in claim 1 wherein the upward movement of molten material and gas from the metal layer into the upper region of the vessel is sufficient to wet water-cooled panels that form a side wall and optionally a roof of the direct smelting vessel to an extent that heat loss through the panels is less than 3000 kW/m 2 of panel.

9. The process defined in claim 1 wherein the upward movement of molten material and gas from the metal layer into the upper region of the vessel is sufficient to cause substantial agitation in the molten bath and facilitate heat transfer from the upper region into the molten bath.

10. The process defined in claim 1 comprising injecting the carbonaceous material through at least one additional lance into the direct smelting vessel during the process.

11. The process defined in claim 1 comprising injecting at least 100 tonnes/hour iron ore and at least 60 tonnes/hour coal into the direct smelting vessel and producing at least 60 tonnes/hour molten iron.

12. The process defined in claim 1 comprising operating in a range of pressures between 0.6 to 1.0 barg.

13. The process defined in claim 1 wherein the upward movement of molten material and gas from the metal layer into the upper region of the vessel is sufficient to wet water-cooled panels that form a side wall and optionally a roof of the direct smelting vessel to an extent that heat loss through the panels is less than 2000 kW/m 2 of panel.

14. A molten bath-based process for direct smelting metalliferous material and producing molten metal in a direct smelting vessel having a vessel floor and an upper region, which process comprises pneumatically injecting a solid metalliferous material and a solid carbonaceous material through at least one pair of opposed injection lances extending downwardly and inwardly into a molten bath in the direct smelting vessel, longitudinal axes of the lances intersecting within a top three quarters of a metal layer in the molten bath, as measured from the vessel floor, and selecting momentum and/or the velocity of the injected material to penetrate the molten bath whereby plumes of pneumatically injected material from the lances coalesce in the molten bath below a nominal interface of molten metal and molten slag under quiescent conditions, thereby producing significant upward movement of molten material and gas from the metal layer of the molten bath.

15. The process defined in claim 14 wherein the momentum of the injected material is at least one selected from the group consisting of average momentum of gas, metalliferous material, and carbonaceous material forming the plumes.

Assignees

• Pilote Jacques
• Dry Rodney James
• Tech Resources Pty Ltd

Inventors

• Pilote Jacques
• Dry Rodney James

Classifications

• C21B13/0013 Primary

  introduction of iron oxide into a bath of molten iron containing a carbon reductant · CPC title

• F27D3/18

  Charging particulate material using a fluid carrier · CPC title

• F27B3/22

  Arrangements of air or gas supply devices · CPC title

• C21B13/0026

  introduction of iron oxide in the flame of a burner or a hot gas stream · CPC title

• F27B3/10 Primary

  Details, accessories or equipment, e.g. dust-collectors, specially adapted for hearth-type furnaces · CPC title