Method for producing carrier for electrode catalyst, precursor of carrier for electrode catalyst, and carrier for electrode catalyst, comprising same
US-12057587-B2 · Aug 6, 2024 · US
US2024128475A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024128475-A1 |
| Application number | US-202318204134-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 31, 2023 |
| Priority date | Oct 17, 2022 |
| Publication date | Apr 18, 2024 |
| Grant date | — |
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A manufacturing method of a catalyst may modify a carbon layer structure by using various heat treatment gases such as inert gas (Ar), hydrogen, and carbon monoxide in a carbon layer manufacturing process, thereby optimizing the carbon layer structure according to the purpose of a metal without changing a size of the metal.
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What is claimed is: 1 . A method of manufacturing a catalyst for a fuel cell, the method comprising: (A) obtaining a component including a support and an active metal supported on the support; and (B) obtaining a catalyst by heat-treating the component in a gas atmosphere, wherein the gas atmosphere comprises inert gas, nitrogen (N 2 ), hydrogen (H 2 ), carbon monoxide (CO), or any combination thereof, and wherein the catalyst comprises the support, the active metal supported on the support, and a carbon layer coated on a surface of the active metal. 2 . The method of claim 1 , wherein the gas atmosphere is inert gas comprising argon. 3 . The method of claim 1 , wherein the gas atmosphere is a mixed gas atmosphere comprising nitrogen and hydrogen. 4 . The method of claim 3 , wherein the mixed gas atmosphere comprises nitrogen and hydrogen at a volume ratio in a range of 80:20 to 95:5. 5 . The method of claim 1 , wherein the gas atmosphere comprises carbon monoxide. 6 . The method of claim 1 , wherein the gas atmosphere is a mixed gas atmosphere comprising argon and carbon monoxide. 7 . The method of claim 6 , wherein the mixed gas atmosphere comprises argon and carbon monoxide at a volume ratio in a range of 90:10 to 99:1. 8 . The method of claim 1 , wherein operation (B) comprises: (B-1) primarily heat-treating the component in the gas atmosphere comprising inert gas, nitrogen (N 2 ), hydrogen (H 2 ), carbon monoxide (CO), or any combination thereof; and (B-2) secondarily heat-treating the primarily heat-treated component in the gas atmosphere comprising inert gas, nitrogen (N 2 ), hydrogen (H 2 ), carbon monoxide (CO), or any combination thereof. 9 . The method of claim 8 , wherein the gas atmosphere of operation (B-1) is a mixed gas atmosphere of nitrogen and hydrogen, and wherein the gas atmosphere of operation (B-2) is carbon monoxide. 10 . The method of claim 9 , wherein the mixed gas atmosphere of (B-1) comprises nitrogen and hydrogen at a volume ratio in a range of 80:20 to 95:5. 11 . The method of claim 1 , wherein the catalyst has a particle diameter in a range of 3 nm to 5 nm obtained from Scherrer's equation by using a half width of a peak with respect to a plane 220 of an X-ray diffraction spectrum. 12 . The method of claim 1 , wherein the catalyst has an exposed metal surface area (EMSA) in a range of 0.1 m 2 /g pt to 25 m 2 /g pt . 13 . The method of claim 1 , wherein the catalyst has catalyst activity in an oxygen reduction reaction (ORR) in a range of 0.1V to 0.7V based on −1.5 mA/cm 2 gco . 14 . The method of claim 1 , wherein the catalyst has mass activity in a hydrogen oxidation reaction (HOR) in a range of 0.5 mA/cm 2 gco to 2.0 mA/cm 2 gco based on 0.02V.
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