Electrochemical method for producing pure-oxygen gas and oxygen-lean gas from oxygen-containing gas mixtures
US-10017865-B2 · Jul 10, 2018 · US
US10283780B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10283780-B2 |
| Application number | US-201515527357-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 17, 2015 |
| Priority date | Dec 19, 2014 |
| Publication date | May 7, 2019 |
| Grant date | May 7, 2019 |
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An electrode for use in an electrochemical cell, especially a zinc-bromine flow battery or a hydrogen/bromine flow battery, and methods for manufacturing and using the electrode is provided. The electrode has a metal substrate and a catalytic coating applied onto the substrate wherein the catalytic coating has a Ru-rich mixture of ruthenium and having 70-80 mol % Ru, 1-5 mol % Pt and 17-25 mol % Ir. The catalytic coating composition exhibits a surprisingly high voltage efficiency and operating lifetime despite its relatively low Ir/Ru and Pt/Ru ratios. The underlying metal substrate is for example a porous Ti layer or a layer with titanium suboxides Ti x O y .
Opening claim text (preview).
The invention claimed is: 1. Electrode for use in electrochemical cells comprising: a metal substrate; and a catalytic coating comprising a mixture of noble metals or oxides thereof, wherein said mixture comprises 70-80% ruthenium, 17-25% iridium and 1-5% platinum in mole percentage referred to the elements. 2. The electrode according to claim 1 , wherein the loading of ruthenium, iridium and platinum is 5 to 30 g/m 2 referred to the sum of the elements. 3. The electrode according to claim 1 , wherein said metal substrate consists of a titanium material. 4. The electrode according to claim 3 further comprising an intermediate layer containing titanium material applied between said metal substrate and said catalytic coating. 5. The electrode according to claim 4 , wherein said titanium material comprises titanium suboxides according to the formula Ti x O y , wherein x is in the range of 2 to 10 and y is in the range of 3 to 19. 6. The electrode according to claim 1 , wherein said substrate has an average porosity of 40% to 60%. 7. Method for the production of an electrode according to claim 1 comprising the following sequential steps: applying a precursor solution comprising a mixture of ruthenium, iridium and platinum compounds in one or more coats over said metal substrate; drying said metal substrate after each coating at a temperature of 80° C. to 150° C.; and thermally treating said dried metal substrate at a temperature of 350° C. to 600° C. 8. The method according to claim 7 , wherein the precursor solution is applied to said metal substrate in 3 to 8 coats. 9. Process for energy storage comprising the following steps: circulating a zinc bromide solution within at least one electrochemical cell; and performing the electrolysis of said solution within said electrochemical cell; said electrochemical cell being equipped with at least one electrode comprising a metal substrate and a catalytic coating comprising a mixture of noble metals or oxides thereof, wherein said mixture comprises 60-85% ruthenium, 0-25% iridium and 1-15% platinum in mole percentage referred to the elements, wherein said electrode alternately evolves and reduces bromine. 10. The process according to claim 9 further comprising the execution of a periodic electric charge and discharge cycle on said electrochemical cell by means of an external electric circuit. 11. Flow battery comprising at least one electrode according to claim 1 . 12. Flow battery comprising at least one electrode which alternately evolves and reduces bromine comprising a metal substrate and a catalytic coating comprising a mixture of noble metals or oxides thereof, wherein said mixture comprises 60-85% ruthenium, 0-25% iridium and 1-15% platinum in mole percentage referred to the elements, wherein said flow battery is a zinc/bromine flow battery, a hydrogen/bromine flow battery or an organic redox species/bromine flow battery.
Halogens or compounds thereof · CPC title
Regeneration by electrochemical means · CPC title
Indirect fuel cells, e.g. fuel cells with redox couple being irreversible (H01M8/18 takes precedence) · CPC title
Heat treatment, e.g. drying, baking · CPC title
layered · CPC title
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