Electrocatalyst for acidic media and method of making an electrocatalyst for acidic media
US-2016340791-A1 · Nov 24, 2016 · US
US10167562B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10167562-B2 |
| Application number | US-201615169116-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 31, 2016 |
| Priority date | Jun 1, 2015 |
| Publication date | Jan 1, 2019 |
| Grant date | Jan 1, 2019 |
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A catalyst for an oxygen evolution reaction has a higher and longer-life catalytic activity than that of the conventional and expensive noble metal oxide catalysts, such as RuO 2 and IrO 2 . An A-site ordered perovskite oxide catalyst (such as CaCu 3 Fe 4 O 12 and CaMn 3 Mn 4 O 12 etc.) as an oxygen evolution reaction catalyst is excellent in cost effectiveness. The catalyst has a high catalytic activity compared with a noble metal oxide catalyst, and a long repetition use life since it is extremely stable also under the oxidative reaction conditions. Use of the catalyst is expected to the important energy conversion reactions such as a charge reaction of a metal-air battery, an anode oxygen evolution reaction in the case of a direct water decomposition reaction by sunlight, etc.
Opening claim text (preview).
What is claimed is: 1. A catalyst composition comprising: a catalyst comprising an A-site ordered perovskite oxides. represented by the chemical formula (1): AA' 3 B 4 O 12 , wherein A represents at least one metallic element selected from the group consisting of Na, K, Ca, Sr, Ba, Ag, Pb, Bi, Y, La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb and Lu, A′ represents at least one transition metal element selected from the group consisting of Cu, Mn, Fe, Co and Pd, and forms a covalent bond, and B represents at least one metallic element selected from the group consisting of Ti, V, Cr, Mn, Fe, Co, Ru, Rh, Re, 1 r, Pt, Al, Ga, Ge, Sn and Sb; and a carrier. 2. The catalyst composition according to claim 1 , wherein an ionic radius of the A-site metal ion is larger than an ionic radius of the A′-site metal ion in the A-site ordered perovskite by 0.37Å or more. 3. The catalyst composition according to claim 1 , wherein the A-site ordered perovskite oxide is the A-site ordered perovskite oxide represented by the chemical formula (2): A I Cu 3 Fe 4 O 12 , wherein A I represents at least one metallic element selected from the group consisting of Ca, Sr, Y, La and Ce, and this Cu has a covalent bond. 4. The catalyst composition according to claim 1 , wherein the A-site ordered perovskite oxide is the A-site ordered perovskite oxide represented by the chemical formula (3): CaCu 3 B I 4 O 12 , wherein Cu has a covalent bond and B I is at least one transition metal element selected from the group consisting of Ti, Mn, Fe and Ru. 5. The catalyst composition according to claim 1 , wherein the A-site ordered perovskite oxide is the A-site ordered perovskite oxide which is represented by the chemical formula (4): CaCu 3 Fe 4 O 12 , and this Cu has a covalent bond. 6. The catalyst composition according to claim 1 , wherein the A-site ordered perovskite oxide is an A-site ordered perovskite oxide represented by the chemical formula (5): A II Cu 3 B II 4 O 12 or the chemical formula (6): A II Mn 3 B II 4 O 12 , wherein A II represents at least one metallic element selected from the group consisting of Ca, La, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb and Lu, and B II represents Ti, Mn, Ru or (Fe 0.5 +Sb 0.5 ). 7. The catalyst composition according to claim 6 , wherein the A-site ordered perovskite oxide represented by the chemical formula (5) is CaCu 3 Ti 4 O 12 , CaCu 3 Ru 4 O 12 , CaCu 3 (Fe 2 Sb 2 )O 12 or CaCu 3 (Fe 2 Re 2 )O 12 , or the A-site ordered perovskite oxide represented by the chemical formula (6) is CaMn 3 Mn 4 O 12 . 8. The catalyst composition according to claim 7 wherein the A-site ordered perovskite oxide is produced by an atmospheric pressure synthetic process. 9. The catalyst composition according to claim 1 , wherein the A-site ordered perovskite oxide is produced by a high pressure synthetic process of 1 GPa -20 GPa.
by electrolysis of water · CPC title
Cross-Sectional Technologies · mapped topic
Chemistry & Metallurgy · mapped topic
of the perovskite type · CPC title
Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title
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