Process and apparatus for producing liquid pig iron or liquid primary steel products

Patent metadata

Field	Value
Publication number	US-9139884-B2
Application number	US-92275309-A
Country	US
Kind code	B2
Filing date	Jan 30, 2009
Priority date	Mar 17, 2008
Publication date	Sep 22, 2015
Grant date	Sep 22, 2015

Abstract

A process and an apparatus for producing liquid pig iron or liquid primary steel products from charge materials formed by iron ores and additions. The charge materials are subjected to a further reduction in a reducing zone ( 1 ) and are then fed to a smelting zone or a smelting unit ( 2 ), in particular a fusion gasifier, for smelting with the addition of carbon carriers and oxygen-containing gas to form a fixed bed. A CO- and H 2 -containing reduction gas is formed, which gas is introduced into the reducing zone converted there and drawn off as top gas. The hot top gas, laden with solid matter, after separation of the solids, is subjected at least to a dry coarse separation and at least parts of the hot solids segregated by the separation are returned into the smelting zone or the smelting unit ( 2 ) or the reducing unit ( 1 ). In addition, the top gas is treated in a further fine separation stage ( 13 A).

First claim

The invention claimed is:

1. A process for producing liquid pig iron or liquid primary steel products from charge materials formed by iron ores and additions, the process comprising:
subjecting the charge materials to a reduction in a reducing zone and then feeding the charge materials to a smelting unit for smelting along with adding carbon carriers and oxygen-containing gas to form a fixed bed and for forming a CO- and H 2 -containing reduction gas;
introducing the reduction gas into the reducing zone to form a converted reduction gas, then drawing the converted reduction gas off from the reducing zone as hot top gas;
subjecting the hot top gas, laden with solid matter, to at least a dry dust separation, for at least partially separating the solid matter from the top gas, and returning at least parts of the separated solid matter into the smelting unit or into the reducing zone,
after the dry dust separation, subjecting the top gas at least to an additional fine separation stage for at least partially separating the solid matter remaining in the top gas, and returning the separated solid matter, separated in the fine separation stage, into the smelting unit, the additional fine separation stage being performed by at least two devices, at least two of the at least two devices being connected in parallel to each other, the at least two devices performing the additional fine separation stage further comprising an additional separation device that can be turned on or off.

2. The process as claimed in claim 1 , further comprising, before the returning of the separated solid matter into the smelting unit, and where the separated solid matter contains high proportions of slag-forming constituents, adding to the separated solid matter iron and/or carbon carriers, dried slurries or fine ore, such that the separated solid matter together with the additions has an iron and carbon content of greater than 30%.

3. The process as claimed in claim 1 , further comprising initially treating the separated solid matter to enrich the iron and carbon content thereof, by means of dust classification, hydrocycloning, flotation and/or washing out of water-soluble or readily suspensible components, and then returning the separated solid matter into the smelting unit.

4. The process as claimed in claim 1 , further comprising feeding of the separated solid matter into an upper part of the smelting unit, above the fixed bed.

5. The process as claimed in claim 1 , further comprising segregating particles of solid matter from the reduction gas before introducing the reduction gas into the reducing zone and introducing the particles of solid matter together with the solid matter separated from the top gas into the smelting unit,
wherein an additional separation device, other than a separation device performing the dry dust separation, segregates the particles of solid matter from the reduction gas.

6. The process as claimed in claim 1 , further comprising feeding the separated solid matter to an agglomeration device or burner and then introducing an agglomerate into the smelting unit.

7. The process as claimed in claim 1 , wherein the additional fine separation stage has one or more dry dedusting stages.

8. The process as claimed in claim 1 , wherein the additional fine separation stage has one or more wet dedusting stages.

9. The process as claimed in claim 1 , further comprising passing cleaned top gas to an expansion turbine to make use of compressive energy of the top gas.

10. The process as claimed in claim 1 , further comprising cooling the top gas before and/or after the dry separation by injecting water, steam or cooling gas, wherein the volume of the gas is increased, along with at least partial evaporation of the water.

11. The process as claimed in claim 1 , further comprising, discharging the heat content of the top gas, subjected to at least the dry dust separation, by a heat exchanger and using the heat for at least one of heating process gases or inert gases, drying and/or heating process charge materials or recirculated materials or steam generation.

12. The process as claimed in claim 1 , wherein the smelting unit is a fusion gasifier, and the dry dust separation is a coarse separation.

13. The process as claimed in claim 4 , wherein the separated solid matter is agglomerated in an agglomeration burner and is introduced into the upper part of the smelting unit.

14. The process as claimed in claim 6 , wherein the solid matter is fed with an admixture of fine ores and/or iron carriers and/or carbon carriers to the agglomeration device or burner.

15. A process for producing liquid pig iron or liquid primary steel products from charge materials formed by iron ores and additions, the process comprising:
subjecting the charge materials to a reduction in a reducing zone and then feeding the charge materials to a smelting unit for smelting along with adding carbon carriers and oxygen-containing gas to form a fixed bed and for forming a CO- and H 2 -containing reduction gas;
introducing the reduction gas into the reducing zone to form a converted reduction gas, then drawing the converted reduction gas off from the reducing zone as hot top gas;
subjecting the hot top gas, laden with solid matter, to at least a dry dust separation, for at least partially separating the solid matter from the top gas, and returning at least parts of the separated solid matter into the reducing zone and directly into the smelting unit,
after the dry dust separation, subjecting the top gas at least to an additional fine separation stage for at least partially separating the solid matter remaining in the top gas, and returning the separated solid matter, separated in the fine separation stage, into the smelting unit, the additional fine separation stage being performed by at least two devices, at least two of the at least two devices being connected in parallel to each other.

16. A process for producing liquid pig iron or liquid primary steel products from charge materials formed by iron ores and additions, the process comprising:
subjecting the charge materials to a reduction in a reducing zone and then feeding the charge materials to a smelting unit for smelting along with adding carbon carriers and oxygen-containing gas to form a fixed bed and for forming a CO- and H 2 -containing reduction gas;
introducing the reduction gas into the reducing zone to form a converted reduction gas, then drawing the converted reduction gas off from the reducing zone as hot top gas;
subjecting the hot top gas, laden with solid matter, to at least a dry dust separation, for at least partially separating the solid matter from the top gas, and returning at least parts of the separated solid matter into the smelting unit or into the reducing zone,
after the dry dust separation, subjecting the top gas at least to an additional fine separation stage for at least partially separating the solid matter remaining in the top gas, and returning the separated solid matter, separated in the fine separation stage, into the smelting unit, the additional fine separation stage being performed by at least two devices, at least one of the at least two devices being connected in parallel to the at least two devices, which are different from the at least one device, such that one of the at least one device connected in parallel can be turned on or off.

Assignees

• Aichinger Georg
• Eder Thomas
• Heckmann Hado
• Millner Robert
• Schenk Johannes Leopold
• Schmidt Martin
• Wieder Kurt
• Wurm Johann
• Primetals Technologies Austria GmbH

Inventors

• Aichinger Georg
• Eder Thomas
• Heckmann Hado
• Millner Robert
• Schenk Johannes Leopold
• Schmidt Martin
• Wieder Kurt
• Wurm Johann

Classifications

• C21B2100/66

  Heat exchange · CPC title

• C21B2100/44

  Removing particles, e.g. by scrubbing, dedusting · CPC title

• C21B13/14 Primary

  Multi-stage processes {processes carried out in different vessels or furnaces} · CPC title

• C21B13/002

  Reduction of iron ores by passing through a heated column of carbon · CPC title

• C21B2100/62

  Energy conversion other than by heat exchange, e.g. by use of exhaust gas in energy production · CPC title