Method for the direct reduction of iron ore

Patent metadata

Field	Value
Publication number	US-12286679-B2
Application number	US-202017775419-A
Country	US
Kind code	B2
Filing date	Nov 5, 2020
Priority date	Nov 15, 2019
Publication date	Apr 29, 2025
Grant date	Apr 29, 2025

Abstract

The invention relates to a process for direct reduction of iron ore to afford direct reduced iron, wherein the iron ore sequentially passes through a reduction zone for reducing the iron ore to direct reduced iron and a cooling zone for cooling the direct reduced iron, wherein in the reduction zone the iron ore is subjected to a flow of a reduction gas and wherein in the cooling zone the direct reduced iron is subjected to a flow of a cooling gas. The cooling gas in the cooling zone comprises H2 and CO2, wherein the ratio of the mole fractions of H2 to CO2 is greater than 1.8 and the mole fraction of CO2 is greater than 20 mol %.

First claim

The invention claimed is:

1. A process for direct reduction of iron ore to afford direct reduced iron, wherein the iron ore sequentially passes through a reduction zone for reducing the iron ore to direct reduced iron and a cooling zone for cooling the direct reduced iron, wherein in the reduction zone the iron ore is subjected to a flow of a reduction gas and wherein in the cooling zone the direct reduced iron is subjected to a flow of a cooling gas, wherein the cooling gas in the cooling zone comprises H2 and CO2, wherein the ratio of the mole fractions of H2 to CO2 is greater than 1.8 and less than 2.2 and the mole fraction of CO2 is greater than 20 mol %.

2. The process as claimed in claim 1 , wherein the cooling gas in the cooling zone comprises less than 5 mol % of hydrocarbons.

3. The process as claimed in claim 2 wherein upon entering the cooling zone the direct reduced iron has a temperature in the range from 400° C. to 1100° C.

4. The process as claimed in claim 3 wherein in the cooling zone the cooling gas in the presence of the direct reduced iron as catalyst undergoes a Bosch reaction with the result that carbon is deposited on the direct reduced iron.

5. The process as claimed in claim 4 , wherein the deposited carbon reacts with the iron of the direct reduced iron to form Fe3C.

6. The process as claimed in claim 5 wherein the carbon content of the cooled direct reduced iron is in the range from 0.5% by weight to 4.5% by weight.

7. The process as claimed in claim 6 wherein the reduction zone is arranged above the cooling zone in a shaft furnace and the iron ore passes through the shaft furnace in a vertical direction.

8. The process as claimed in claim 7 , wherein the cooling gas flows through the cooling zone counter to a direction of motion of the iron ore.

9. The process as claimed in claim 6 wherein the reduction zone comprises one or more fluidized bed reactors and the cooling zone ( 15 ) comprises one or more fluidized bed reactors.

10. The process as claimed in claim 9 wherein the reduction gas in the reduction zone contains more than 75 mol % of H2.

11. The process as claimed in claim 9 wherein the reduction gas in the reduction zone contains more than 85 mol % of H2.

12. The process as claimed in claim 11 wherein the reduction gas in the reduction zone comprises less than 5 mol % of hydrocarbons.

13. The process as claimed in claim 11 wherein the reduction gas in the reduction zone comprises less than 2 mol % of hydrocarbons.

14. The process as claimed in claim 1 , wherein the cooling gas in the cooling zone comprises less than 2 mol % of hydrocarbons.

Assignees

• Thyssenkrupp Steel Europe Ag

Inventors

• Weinberg Matthias
• Schubert Daniel

Classifications

• C21B13/0073 Primary

  Selection or treatment of the reducing gases · CPC title

• C21B13/029

  Introducing coolant gas in the shaft furnaces · CPC title

• Y02P10/122

  by capturing or storing CO2 · CPC title

• C21B13/0093

  Protecting against oxidation · CPC title

• C21B13/0033 Primary

  In fluidised bed furnaces or apparatus containing a dispersion of the material · CPC title