US2025327200A1PendingUtilityA1
Electrode for electrolytic evolution of gas
Est. expiryJul 8, 2042(~16 yrs left)· nominal 20-yr term from priority
C25B 1/46C25B 9/19C25B 1/50C25B 11/061C25B 11/093C25B 11/052
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Claims
Abstract
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.
Claims
exact text as granted — not AI-modified1 . 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 .Join the waitlist — get patent alerts
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