IP Library Granted Patent US 10,106,863
Granted Patent B2
US 10,106,863 · App. 15/110,073 · Granted Oct 23, 2018

Method for operation of blast furnace

Inventors: Takanobu Inada (Tokyo, JP); Hiroshi Sakai (Tokyo, JP); Yutaka Ujisawa (Tokyo, JP)
Assignees: NIPPON STEEL & SUMITOMO METAL CORPORATION; JFE STEEL CORPORATION; KOBE STEEL, LTD.; NISSHIN STEEL CO., LTD.; NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD.
C21B5/003C21B5/001C21B5/06C21B7/002C21B7/16F27B1/10C21B2100/02C21B2100/04C21B2100/282Y02P10/122Y02P10/143Y02P10/283
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Quick Facts
Patent No.
US 10,106,863
App. No.
15/110,073
Granted
Oct 23, 2018
Kind
B2
Abstract

A method for operation of a blast furnace able to greatly reduce the CO 2 emission and enabling stable production of pig iron over a long period of time in a commercial blast furnace, that is, a method for operation of a blast furnace in which iron ore and coke are charged from a furnace top and is blown in pulverized coal from a usual tuyere, comprising blowing in a gas containing at least one of hydrogen and hydrocarbon from the usual tuyere together with the pulverized coal and blowing a gas comprised of a top gas of the blast furnace from which carbon dioxide and steam is removed from a shaft tuyere into the blast furnace.

Claims (21)

1. A method for operation of a blast furnace in which iron ore and coke are charged from a furnace top and pulverized coal is injected from a usual tuyere provided at a lower stage of the furnace at the side below a shaft tuyere, comprising

blowing a blast containing at least one of hydrogen and hydrocarbon from said usual tuyere together with said pulverized coal,

blowing a gas comprised of a first part of a top gas of the blast furnace from which carbon dioxide and steam are removed from the shaft tuyere into the blast furnace,

blowing a second part of said top gas from the usual tuyere without heating the second part thereof, and

raising an oxygen enrichment of gas blown from the usual tuyere,

wherein said blast from the usual tuyere is enriched with oxygen by an oxygen enrichment of 10% not less than and not more than by a Y % shown in the following formula:

Y= 0.079×CH 4 +32

wherein CH 4 indicates a vol % of methane in the blast blown in from the usual tuyere, and the vol % of the blast blown in from the usual tuyere is in a range from 0 to 100.

2. The method for operation of a blast furnace according to claim 1 , further comprising blowing a gas comprised of the second part of the top gas of the blast furnace from which carbon dioxide and steam are removed from the usual tuyere into the blast furnace.

3. The method for operation of a blast furnace according to claim 1 , wherein a blowing rate of the blast containing at least one of hydrogen and hydrocarbon is 30 Nm 3 /tHM or more.

4. The method for operation of a blast furnace according to claim 1 , wherein said top gas blown from the shaft tuyere is blown from said shaft tuyere by a blowing rate of 400 Nm 3 /tHM or less at a temperature of 600° C. to 1000° C.

5. The method for operation of a blast furnace according to claim 1 , wherein the blowing rate of the top gas blown from said shaft tuyere is 100 Nm 3 /tHM or more.

6. The method for operation of a blast furnace according to claim 1 , wherein the blast containing at least one of hydrogen and hydrocarbon blown from said usual tuyere contains methane.

7. The method for operation of a blast furnace according to claim 6 , wherein the blast containing methane includes at least one of coke oven gas and natural gas.

8. The method for operation of a blast furnace according to claim 2 , wherein a blowing rate of the blast containing at least one of hydrogen and hydrocarbon is 30 Nm 3 /tHM or more.

9. The method for operation of a blast furnace according to claim 2 , wherein said top gas blown from the shaft tuyere is blown from said shaft tuyere by a blowing rate of 400 Nm 3 /tHM or less at a temperature of 600° C. to 1000° C.

10. The method for operation of a blast furnace according to claim 3 , wherein said top gas blown from the shaft tuyere is blown from said shaft tuyere by a blowing rate of 400 Nm 3 /tHM or less at a temperature of 600° C. to 1000° C.

11. The method for operation of a blast furnace according to claim 2 , wherein the blowing rate of the top gas blown from said shaft tuyere is 100 Nm 3 /tHM or more.

12. The method for operation of a blast furnace according to claim 3 , wherein the blowing rate of the top gas blown from said shaft tuyere is 100 Nm 3 /tHM or more.

13. The method for operation of a blast furnace according to claim 4 , wherein the blowing rate of the top gas blown from said shaft tuyere is 100 Nm 3 /tHM or more.

14. The method for operation of a blast furnace according to claim 2 , wherein the blast containing at least one of hydrogen and hydrocarbon blown from said usual tuyere contains methane.

Assignments (3)
CHANGE OF NAME Recorded Jan 13, 2020
From: NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD.
To: NIPPON STEEL ENGINEERING CO., LTD.
Reel/Frame 051569/0634 →
CHANGE OF NAME Recorded May 14, 2019
From: NIPPON STEEL & SUMITOMO METAL CORPORATION
To: NIPPON STEEL CORPORATION
Reel/Frame 049257/0828 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 8, 2016
From: INADA, TAKANOBU; SAKAI, HIROSHI; UJISAWA, YUTAKA
To: NIPPON STEEL & SUMITOMO METAL CORPORATION; JFE STEEL CORPORATION; KABUSHIKI KAISHA KOBE SEIKO SHO (KOBE STEEL, LTD.); NISSHIN STEEL CO., LTD.; NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD.
Reel/Frame 039111/0846 →
Priority Claims (1)
JP 2014-000901 · Jan 7, 2014 · national
Continuity (1)
Related Publication 20160326604A1 · Nov 10, 2016
Cited By (1)
US 12,365,953