Electrolysis cell and electrolysis tank
US-9506157-B2 · Nov 29, 2016 · US
US2025327200A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025327200-A1 |
| Application number | US-202318868246-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 6, 2023 |
| Priority date | Jul 8, 2022 |
| Publication date | Oct 23, 2025 |
| Grant date | — |
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An electrode for gas evolution in electrolytic processes comprising a catalytic coating containing oxides of tin, ruthenium, titanium and one or more elements selected from the group consisting of niobium, tantalum and tungsten applied to a metallic substrate, and a method for its preparation.
Opening claim text (preview).
1 . An electrode for gas evolution in electrolytic processes comprising a metal substrate and a catalytic coating said catalytic coating comprising tin, ruthenium, titanium and one or more elements selected from the group consisting of niobium, tantalum, tungsten wherein tin is 10-20%, ruthenium is 25-45%, titanium is 20-40%, and one or more elements selected from the group consisting of niobium, tantalum, tungsten is 10-20% in the form of metals or their oxides in percentage by weight referred to the elements. 2 . The electrode according to claim 1 wherein said one or more elements selected from the group consisting of niobium, tantalum, tungsten is tantalum. 3 . The electrode according to claim 1 wherein the titanium of said catalytic coating is present in the form of oxide in the rutile form. 4 . The electrode according to claim 1 wherein the catalytic coating has a ruthenium load comprised between 2.2 and 9 g/m 2 . 5 . A method for the production of an electrode as defined in claim 1 , comprising the following steps: a) applying to a metal substrate a solution comprising the precursors of ruthenium, tin, titanium and one or more elements selected from the group consisting of niobium, tantalum, tungsten, subsequent drying at 50-60° C. and thermal decomposition at 450-600° C. for a time of 5 to 30 minutes until reaching a specific load of ruthenium comprised between 0.4 and 1.2 g/m 2 ; b) repeating step a) until obtaining a catalytic coating with a specific load of ruthenium comprised between 2.2 and 9 g/m 2 ; c) thermally treating at 450-600° C. for a time of 50 to 200 minutes. 6 . A cell for the electrolysis of alkaline chloride solutions and/or for electro-chlorination comprising an anodic compartment and a cathodic compartment wherein the anodic compartment is equipped with the electrode according to claim 1 . 7 . The cell for electrolysis and/or for electro-chlorination according to claim 6 wherein said anodic compartment and said cathodic compartment are separated by a diaphragm or an ion exchange membrane. 8 . An electrolyzer for the production of chlorine and alkali starting from alkali chloride solutions comprising a modular arrangement of cells according to claim 7 .
in diaphragm cells · CPC title
with diaphragms · CPC title
Processes · CPC title
Metal or alloy · CPC title
at least one noble metal or noble metal oxide and at least one non-noble metal oxide · CPC title
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