Alternative low cost electrodes for hybrid flow batteries
US-2024047707-A1 · Feb 8, 2024 · US
US2021288335A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021288335-A1 |
| Application number | US-202017107272-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 30, 2020 |
| Priority date | Mar 13, 2020 |
| Publication date | Sep 16, 2021 |
| Grant date | — |
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Disclose is a method of manufacturing catalyst ink for a fuel cell, and particularly the method includes removing eluted transition metal from a noble-metal/transition-metal alloy catalyst.
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What is claimed is: 1 . A method of manufacturing catalyst ink for a fuel cell, comprising: admixing 1) an alloy catalyst comprising a noble metal and a transition metal and 2) polymer particles, whereby an aggregate comprising i) the transition metal and ii) polymer particles forms. 2 . The method of claim 1 wherein an admixture is provided comprising an alloy catalyst comprising a noble metal and a transition metal, an ionomer and a solvent; and the admixture and polymer particles to form an aggregate comprising 1) the transition metal associated with the alloy catalyst and 2) the polymer particles. 3 . The method of claim 2 wherein the aggregate is removed by filtration. 4 . The method of claim 2 , wherein the noble metal comprises one or more selected from the group consisting of platinum (Pt), iridium (Ir), palladium (Pd), ruthenium (Ru), rhodium (Rd), gold (Au), ad silver (Ag). 5 . The method of claim 2 , wherein the transition metal comprises one or more selected from the group consisting of cobalt (Co), nickel (Ni), yttrium (Y), chromium (Cr), manganese (Mn), copper (Cu), lanthanum (La), and scandium (Sc). 6 . The method of claim 2 , wherein the alloy catalyst is supported on a support. 7 . The method of claim 2 , wherein the polymer particles comprise a chelating resin. 8 . The method of claim 2 , wherein the polymer particles comprise, as a side chain, one or more chelating formation groups selected from the group consisting of glutamine, amidoxime, thiol, iminodiacetic acid, aminophosphonic acid, phosphonic acid, sulfonic acid, polyamine, thiourea, aminomethyl phosphonic acid, benzylamine, tertiary amine, and derivatives thereof. 9 . The method of claim 2 , wherein the polymer particles comprises one or more selected from the group consisting of an iminodiacetic-acid-type chelating resin, and an aminophosphonic-acid-type chelating resin. 10 . The method of claim 2 , wherein the polymer particles have an average diameter ranging from about 300 μm to about 800 μm. 11 . The method of claim 2 , wherein the admixture is added with the polymer particles and allowed to react at a temperature of about 25° C. to about 60° C. for about 10 hr to 30 hr to afford an aggregate of the transition metal and the polymer particles. 12 . The method of claim 2 , wherein the aggregate is removed by filtering the admixture using a filter of 32 mesh to 400 mesh. 13 . A method of manufacturing an electrode for a fuel cell, comprising: preparing catalyst ink manufactured by a method of claim 1 ; and forming a catalyst layer by applying the catalyst ink on a substrate and performing drying. 14 . A method of manufacturing an electrode for a fuel cell, comprising: preparing catalyst ink manufactured by a method of claim 2 ; and forming a catalyst layer by applying the catalyst ink on a substrate and performing drying.
Manganese · CPC title
Chromium · CPC title
with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title
with rare earths or actinides · CPC title
combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 · CPC title
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