JP2022115842A5 - - Google Patents

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JP2022115842A5
JP2022115842A5 JP2022011195A JP2022011195A JP2022115842A5 JP 2022115842 A5 JP2022115842 A5 JP 2022115842A5 JP 2022011195 A JP2022011195 A JP 2022011195A JP 2022011195 A JP2022011195 A JP 2022011195A JP 2022115842 A5 JP2022115842 A5 JP 2022115842A5
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carbon
iron
producing
reducing agent
magnetite
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Priority to US18/272,848 priority Critical patent/US20240083750A1/en
Priority to CN202280009206.3A priority patent/CN116685389A/en
Priority to EP22746055.7A priority patent/EP4286326A1/en
Priority to PCT/JP2022/003437 priority patent/WO2022163836A1/en
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上記課題を解決するために、この発明は以下の手段を提案している。
即ち、本発明の炭素材料の製造方法は、二酸化炭素と還元剤とを反応させて炭素を生成する炭素生成工程を有し、前記還元剤は、結晶構造を維持したままマグネタイトを還元することで得られる、Fe4-δ(但し、δは1以上4未満)で表される酸素欠陥鉄酸化物、またはマグネタイトを完全に還元することで得られる、酸素完全欠陥鉄(δ=4)を用い、前記炭素生成工程を経た酸化された前記還元剤の少なくとも一部を、前記製鉄プラントで消費される製鉄原料として前記製鉄プラントに供給する工程を有することを特徴とする。
In order to solve the above problems, the present invention proposes the following means.
That is, the method for producing a carbon material of the present invention has a carbon generation step of reacting carbon dioxide with a reducing agent to generate carbon, and the reducing agent reduces magnetite while maintaining its crystal structure. Oxygen-deficient iron oxide represented by Fe 3 O 4-δ (where δ is 1 or more and less than 4) or completely oxygen-defective iron (δ=4) obtained by completely reducing magnetite and supplying at least part of the oxidized reducing agent that has undergone the carbon generation step to the iron manufacturing plant as an iron manufacturing raw material to be consumed in the iron manufacturing plant .

本発明の二酸化炭素の分解方法は、二酸化炭素と還元剤とを反応させて二酸化炭素を分解する二酸化炭素分解工程を有し、前記二酸化炭素は、製鉄プラントにおいて発生した排出ガスを用い、前記還元剤は、結晶構造を維持したままマグネタイトを還元することで得られる、Fe3O4-δ(但し、δは1以上4未満)で表される酸素欠陥鉄酸化物、またはマグネタイトを完全に還元することで得られる、酸素完全欠陥鉄(δ=4)を用い、前記炭素生成工程を経た酸化された前記還元剤の少なくとも一部を、前記製鉄プラントで消費される製鉄原料として前記製鉄プラントに供給する工程を有することを特徴とする。 The carbon dioxide decomposition method of the present invention has a carbon dioxide decomposition step of reacting carbon dioxide and a reducing agent to decompose carbon dioxide, and the carbon dioxide is generated by using the exhaust gas generated in a steel plant, and the reduction The agent is an oxygen-deficient iron oxide represented by Fe3O4-δ (where δ is 1 or more and less than 4) obtained by reducing magnetite while maintaining the crystal structure, or by completely reducing magnetite. A step of using the obtained oxygen-completely deficient iron (δ=4) and supplying at least part of the oxidized reducing agent that has undergone the carbon generation step to the iron manufacturing plant as a raw material for iron manufacturing that is consumed in the iron manufacturing plant. characterized by having

Claims (14)

二酸化炭素と還元剤とを反応させて炭素とマグネタイトとを生成する炭素生成工程と、前記マグネタイトと水素とを反応させて、前記還元剤を生成する還元剤生成工程と、を有し、
少なくとも前記二酸化炭素または前記水素のいずれか一方のうち、少なくとも一部は、製鉄プラントにおいて発生した排出ガスを用い、
前記還元剤は、結晶構造を維持したままマグネタイトを還元することで得られる、Fe4-δ(但し、δは1以上4未満)で表される酸素欠陥鉄酸化物、またはマグネタイトを完全に還元することで得られる、酸素完全欠陥鉄(δ=4)を用い
前記炭素生成工程を経た酸化された前記還元剤の少なくとも一部を、前記製鉄プラントで消費される製鉄原料として前記製鉄プラントに供給する工程を有することを特徴とする炭素材料の製造方法。
A carbon generation step of reacting carbon dioxide and a reducing agent to generate carbon and magnetite, and a reducing agent generation step of reacting the magnetite and hydrogen to generate the reducing agent,
At least a portion of at least one of the carbon dioxide and the hydrogen uses exhaust gas generated in a steel plant,
The reducing agent is an oxygen-deficient iron oxide represented by Fe 3 O 4-δ (where δ is 1 or more and less than 4) obtained by reducing magnetite while maintaining its crystal structure, or magnetite completely. Using oxygen-completely deficient iron (δ = 4) obtained by reducing to
A method for producing a carbon material , comprising a step of supplying at least part of the oxidized reducing agent that has undergone the carbon generation step to the iron-making plant as an iron-making raw material to be consumed in the iron-making plant .
前記還元剤生成工程は、反応温度が300℃以上、450℃以下の範囲であり、前記製鉄プラントにおいて発生した排熱を用いて加熱を行うことを特徴とする請求項1に記載の炭素材料の製造方法。 The carbon material according to claim 1, wherein the reducing agent generation step has a reaction temperature in the range of 300 ° C. or higher and 450 ° C. or lower, and heating is performed using exhaust heat generated in the iron manufacturing plant. Production method. 前記還元剤生成工程で用いる水素の濃度は5体積%以上、100体積%以下の範囲であることを特徴とする請求項1または2に記載の炭素材料の製造方法。 3. The method for producing a carbon material according to claim 1, wherein the concentration of hydrogen used in said reducing agent generation step is in the range of 5% by volume or more and 100% by volume or less. 前記炭素生成工程は、反応温度が300℃以上、450℃以下の範囲であり、前記製鉄プラントにおいて発生した排熱を用いて加熱を行うことを特徴とする請求項1から3のいずれか一項に記載の炭素材料の製造方法。 4. The carbon production step according to any one of claims 1 to 3, wherein the reaction temperature is in the range of 300° C. or higher and 450° C. or lower, and heating is performed using exhaust heat generated in the iron manufacturing plant. The method for producing the carbon material according to 1. 前記炭素生成工程は、反応圧力が0.01MPa以上、5MPa以下の範囲であることを特徴とする請求項1から4のいずれか一項に記載の炭素材料の製造方法。 The method for producing a carbon material according to any one of claims 1 to 4, wherein the reaction pressure in the carbon generation step is in the range of 0.01 MPa or more and 5 MPa or less. 前記炭素は、粒子径が1μm以下のナノサイズの炭素であることを特徴とする請求項1から5のいずれか一項に記載の炭素材料の製造方法。 The method for producing a carbon material according to any one of claims 1 to 5, wherein the carbon is nano-sized carbon having a particle size of 1 µm or less. 前記マグネタイトの少なくとも一部は、前記製鉄プラントで用いられる鉄鉱石に含まれる砂鉄を用いることを特徴とする請求項1から6のいずれか一項に記載の炭素材料の製造方法。 The method for producing a carbon material according to any one of claims 1 to 6, wherein at least part of the magnetite is iron sand contained in iron ore used in the iron manufacturing plant. 前記炭素生成工程で生成された前記炭素の少なくとも一部を、前記製鉄プラントで消費されるコークスの代替品として前記製鉄プラントに供給する工程を有することを特徴とする請求項1からのいずれか一項に記載の炭素材料の製造方法。 8. The method according to any one of claims 1 to 7 , further comprising a step of supplying at least part of the carbon produced in the carbon production step to the iron plant as a substitute for coke consumed in the iron plant. A method for producing the carbon material according to item 1. 前記炭素生成工程の後工程であって、酸化された前記還元剤を溶解して、前記炭素を分離する炭素回収工程を更に有することを特徴とする請求項1からのいずれか一項に記載の炭素材料の製造方法。 9. The method according to any one of claims 1 to 8 , further comprising a carbon recovery step, which is a step after the carbon generation step and dissolving the oxidized reducing agent to separate the carbon. A method for producing a carbon material. 前記マグネタイトは、BET法による比表面積が0.1m/g以上、10m/g以下の範囲であることを特徴とする請求項1からのいずれか一項に記載の炭素材料の製造方法。 The method for producing a carbon material according to any one of claims 1 to 9 , wherein the magnetite has a specific surface area of 0.1 m 2 /g or more and 10 m 2 /g or less by the BET method. . 前記マグネタイトは、平均粒子径が1μm以上、1000μm以下の範囲であることを特徴とする請求項1から10のいずれか一項に記載の炭素材料の製造方法。 The method for producing a carbon material according to any one of claims 1 to 10 , wherein the magnetite has an average particle size in the range of 1 µm or more and 1000 µm or less. 前記マグネタイトは、かさ密度が0.3g/cm以上、3g/cm以下の範囲であることを特徴とする請求項1から11のいずれか一項に記載の炭素材料の製造方法。 The method for producing a carbon material according to any one of claims 1 to 11 , wherein the magnetite has a bulk density in the range of 0.3 g/ cm3 to 3 g/cm3. 請求項1から12のいずれか一項に記載の炭素材料の製造方法で製造したことを特徴とする炭素材料。 A carbon material produced by the method for producing a carbon material according to any one of claims 1 to 12 . 二酸化炭素と還元剤とを反応させて二酸化炭素を分解する二酸化炭素分解工程を有し、
前記二酸化炭素は、製鉄プラントにおいて発生した排出ガスを用い、
前記還元剤は、結晶構造を維持したままマグネタイトを還元することで得られる、Fe4-δ(但し、δは1以上4未満)で表される酸素欠陥鉄酸化物、またはマグネタイトを完全に還元することで得られる、酸素完全欠陥鉄(δ=4)を用い
前記二酸化炭素分解工程で酸化された前記還元剤の少なくとも一部を、前記製鉄プラントで消費される製鉄原料として前記製鉄プラントに供給することを特徴とする二酸化炭素の分解方法。
Having a carbon dioxide decomposition step of reacting carbon dioxide and a reducing agent to decompose carbon dioxide,
The carbon dioxide uses exhaust gas generated in a steel plant,
The reducing agent is an oxygen-deficient iron oxide represented by Fe 3 O 4-δ (where δ is 1 or more and less than 4) obtained by reducing magnetite while maintaining its crystal structure, or magnetite completely. Using oxygen-completely deficient iron (δ = 4) obtained by reducing to
A method for decomposing carbon dioxide, wherein at least part of the reducing agent oxidized in the carbon dioxide decomposition step is supplied to the iron manufacturing plant as a raw material for iron manufacturing that is consumed in the iron manufacturing plant .
JP2022011195A 2021-01-28 2022-01-27 Method for producing carbon material, carbon material, method for decomposing carbon dioxide Active JP7227544B2 (en)

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US18/272,848 US20240083750A1 (en) 2021-01-28 2022-01-28 Method for producing carbon material, carbon material, method for decomposing carbon dioxide, and reducing agent
CN202280009206.3A CN116685389A (en) 2021-01-28 2022-01-28 Method for producing carbon material, method for decomposing carbon dioxide, and reducing agent
EP22746055.7A EP4286326A1 (en) 2021-01-28 2022-01-28 Method for producing carbon material, carbon material, method for decomposing carbon dioxide, and reducing agent
PCT/JP2022/003437 WO2022163836A1 (en) 2021-01-28 2022-01-28 Method for producing carbon material, carbon material, method for decomposing carbon dioxide, and reducing agent

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JP7367809B2 (en) 2021-06-29 2023-10-24 三菱マテリアル株式会社 Carbon and hydrogen production methods, carbon materials, reducing agents, carbon dioxide decomposition methods
EP4365127A1 (en) * 2021-06-29 2024-05-08 Mitsubishi Materials Corporation Method for producing carbon and hydrogen, carbon material, reducing agent, and method for decomposing carbon dioxide

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