Blast furnace operation method

Patent metadata

Field	Value
Publication number	US-12180555-B2
Application number	US-202017430657-A
Country	US
Kind code	B2
Filing date	Feb 17, 2020
Priority date	Feb 18, 2019
Publication date	Dec 31, 2024
Grant date	Dec 31, 2024

Abstract

A blast furnace operation method according to one aspect of the present invention includes: a process of acquiring a correlation between a carbon consumption in reducing gas and a reduction InputΔC in specific carbon consumption caused by blowing the reducing gas into the blast furnace per molar ratio C/H of carbon atoms to hydrogen atoms in the reducing gas; a process of determining a carbon consumption in the reducing gas where the reduction InputΔC in specific carbon consumption is a predetermined target value or higher on the basis of the correlation acquired per C/H; and a process of adjusting the amount of the reducing gas blown into the blast furnace on the basis of the determined carbon consumption in the reducing gas and the carbon proportion in the reducing gas.

First claim

What is claimed is:

1. A blast furnace operation method in which reducing gas including hydrogen atoms and carbon atoms is blown into a blast furnace, the method comprising:
acquiring a correlation between a carbon consumption in the reducing gas and a reduction InputΔC by performing calculation using instances where molar ratio C/H in the reducing gas and an amount of the reducing gas blown are different from each other,
wherein the InputΔC is defined as a proportion of reduction in specific carbon consumption Input C of an operation where a predetermined amount of reducing gas is blown with respect to a base operation where the reducing gas is not blown, and the Input C refers to the total mass of coke, pulverized coal, and carbon in the reducing gas for producing one ton of molten iron;
determining a carbon consumption in the reducing gas where the reduction InputΔC in specific carbon consumption is a predetermined target value of the reduction InputΔC or higher on the basis of the correlation between the carbon consumption in the reducing gas and the reduction InputΔC acquired per the molar ratio C/H; and
adjusting an amount of the reducing gas blown into the blast furnace on the basis of the determined carbon consumption in the reducing gas and a carbon proportion in the reducing gas,
wherein the carbon consumption in the reducing gas is a value obtained by multiplying a carbon proportion kg/Nm 3 in the reducing gas by the reducing gas volume Nm 3 /t-pig per ton of molten iron.

2. The blast furnace operation method according to claim 1 ,
wherein the molar ratio C/H of the carbon atoms to the hydrogen atoms in the reducing gas is 0.15 or higher.

3. The blast furnace operation method according to claim 2 ,
wherein the correlation is represented by a quadratic expression of the carbon consumption in the reducing gas.

4. The blast furnace operation method according to claim 3 ,
wherein the correlation is represented by Y=a1X 2 +b1X+c1, (where X represents the carbon consumption in the reducing gas, Y represents the reduction InputΔC in specific carbon consumption, and all the coefficients a1, b1, and cl represent values that do not depend on the molar ratio C/H.

5. The blast furnace operation method according to claim 4 ,
wherein the carbon consumption in the reducing gas is determined in a range of 21 kg/t-pig to 107 kg/t-pig.

6. The blast furnace operation method according to claim 4 ,
wherein the carbon consumption in the reducing gas is determined in a range of 21 kg/t-pig to 65 kg/t-pig.

7. The blast furnace operation method according to claim 1 ,
wherein the molar ratio C/H of the carbon atoms to the hydrogen atoms in the reducing gas is higher than 0 and lower than 0.15.

8. The blast furnace operation method according to claim 7 ,
wherein the molar ratio C/H of the carbon atoms to the hydrogen atoms in the reducing gas is 0.13 or lower.

9. The blast furnace operation method according to claim 7 ,
wherein the molar ratio C/H of the carbon atoms to the hydrogen atoms in the reducing gas is 0.10 or lower.

10. The blast furnace operation method according to claim 7 ,
wherein the correlation is represented by Y=a2X 2 +b2X+c2, (where X represents the carbon consumption in the reducing gas, Y represents the reduction InputΔC in specific carbon consumption, and at least one of the coefficients a2, b2, and c2 represents a function including the molar ratio C/H as a variable.

11. The blast furnace operation method according to claim 1 ,
wherein when the reducing gas is blown into the blast furnace, a flame temperature is adjusted to be 2000° C. or higher.

12. The blast furnace operation method according to claim 11 ,
wherein in order to adjust the flame temperature to be 2000° C. or higher, at least one of an blast volume or an oxygen enrichment in hot blast is adjusted.

13. The blast furnace operation method according to claim 1 ,
wherein the reducing gas is coke oven gas, natural gas, reformed top gas gas, city gas, mixed gas thereof, or hydrogen mixed gas obtained by mixing hydrogen gas therewith.

Assignees

• Nippon Steel Corp
• Jfe Steel Corp
• Kobe Steel Ltd
• Nippon Steel Eng Co Ltd

Inventors

• Sakai Hiroshi
• Nishioka Koki
• Nakano Kaoru

Classifications

• F27B14/143

  Heating of the crucible by convection of combustion gases · CPC title

• C21B2300/04

  Modeling of the process, e.g. for control purposes; CII · CPC title

• C21B2005/005

  Selection or treatment of the reducing gases · CPC title

• C21B5/001 Primary

  Injecting additional fuel or reducing agents · CPC title

• Y02P10/143

  of methane [CH4] · CPC title