IP Library › Granted Patent US 12,528,701
Granted Patent B2
US 12,528,701 · App. 17/916,680 · Granted Jan 20, 2026

Solid carbon production device and solid carbon production method

Inventors: Takuya Hirata (Tokyo, JP); Kouji Horizoe (Tokyo, JP)
Assignee: MITSUBISHI HEAVY INDUSTRIES, LTD.
C01B32/05B01J19/0013B01J19/245C01B3/24C21B5/007C21B5/06C21B7/002B01J2219/00135B01J2219/00157C01B2203/0272C01B2203/06C01B2203/0811C01B2203/1241C21B2100/282
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Quick Facts
Patent No.
US 12,528,701
App. No.
17/916,680
Granted
Jan 20, 2026
Kind
B2
Abstract

Provided is a solid carbon production facility including: a separation facility configured to separate a carbon dioxide gas contained in a produced gas produced by a blast furnace; a reaction facility configured to heat a fuel gas whose main component is a methane gas by using a heating facility and decompose the methane gas into solid carbon and a hydrogen gas; and a production facility configured to cause the carbon dioxide gas separated by the separation facility and the hydrogen gas decomposed by the reaction facility to react with each other to produce solid carbon and water.

Claims (16)

1 . A solid carbon production device comprising:

a separation unit configured to separate a carbon dioxide gas contained in a produced gas produced by a blast furnace;

a reaction unit configured to heat a fuel gas whose main component is a methane gas by using a heating source and decompose the methane gas into solid carbon and a hydrogen gas; and

a production unit configured to cause the carbon dioxide gas separated by the separation unit and the hydrogen gas decomposed by the reaction unit to react with each other to produce solid carbon and water.

2 . The solid carbon production device according to claim 1 further comprising a fuel gas supply unit configured to supply the fuel gas to the reaction unit and the heating source,

wherein the heating source is configured to heat the fuel gas supplied from the fuel gas supply unit to the reaction unit by combusting the fuel gas supplied from the fuel gas supply unit.

3 . The solid carbon production device according to claim 2 further comprising a combustion gas supply unit configured to supply the separation unit with a combustion gas produced by combusting the fuel gas by using the heating source.

4 . The solid carbon production device according to claim 1 , wherein the heating source converts electric power into heat to heat the fuel gas.

5 . The solid carbon production device according to claim 1 further comprising a solid carbon supply line configured to supply the blast furnace with solid carbon decomposed by the reaction unit and solid carbon produced by the production unit.

6 . The solid carbon production device according to claim 5 , wherein the solid carbon supply line is configured to supply solid carbon decomposed by the reaction unit and solid carbon produced by the production unit to both a feedstock supply port from which iron ore and coke are supplied to the blast furnace and a pulverized coal supply port from which pulverized coal is supplied to the blast furnace.

7 . The solid carbon production device according to claim 5 , wherein the solid carbon supply line is configured to supply the whole amount of solid carbon decomposed by the reaction unit and solid carbon produced by the production unit to a pulverized coal supply port from which pulverized coal is supplied to the blast furnace.

8 . The solid carbon production device according to claim 5 further comprising a solid molding unit provided to the solid carbon supply line and configured to mix solid carbon decomposed by the reaction unit and solid carbon produced by the production unit with a binder to mold a granular solid carbonaceous material.

9 . A solid carbon production method comprising:

a separation step of separating a carbon dioxide gas contained in a produced gas produced by a blast furnace;

a reaction step of heating a fuel gas whose main component is a methane gas by using a heating source and decomposing the methane gas into solid carbon and a hydrogen gas; and

a production step of causing the carbon dioxide gas separated by the separation step and the hydrogen gas decomposed by the reaction step to react with each other to produce solid carbon and water.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 4, 2022
From: HIRATA, TAKUYA; HORIZOE, KOUJI
To: MITSUBISHI HEAVY INDUSTRIES, LTD.
Reel/Frame 061307/0336 →
Priority Claims (1)
JP 2020-068427 · Apr 6, 2020 · national
Continuity (1)
Related Publication 20230150820A1 · May 18, 2023
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