Process for the production of ammonia from air and water
US-2017037521-A1 · Feb 9, 2017 · US
US2023151503A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023151503-A1 |
| Application number | US-202117906429-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 23, 2021 |
| Priority date | Mar 24, 2020 |
| Publication date | May 18, 2023 |
| Grant date | — |
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A method for surface treatment of a metal substrate, suitable for use as electrode support in electrochemical processes by: (a) immersion of the metal substrate and of at least one counter electrode in an electrolyte selected from hydrochloric acid, nitric acid, boric acid or sulfuric acid at a weight concentration of between 10-40%; (b) application of an anodic current density to the metal substrate of between 0.1 and 30 A/dm2 for a time of between 0.5 and 120 minutes. An electrode for gas evolution in electrochemical processes obtained from a correspondingly treated substrate.
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1 . A method for surface treatment of a metal substrate selected from nickel or nickel alloy, suitable for use as electrode support in electrochemical processes, comprising the following steps: (a) immersing said metal substrate and at least one counter electrode in an electrolyte selected from hydrochloric acid, nitric acid, boric acid or sulfuric acid at a weight concentration of between 10-40%; (b) applying an anodic current density to said metal substrate between 0.1 and 30 A/dm 2 for a time between 0.5 and 120 minutes. 2 . The method according claim 1 wherein said metal substrate is a mesh or a punched or expanded sheet. 3 . The method according to claim 1 wherein said metal substrate has a thickness below 1.2 mm. 4 . The method according to claim 3 wherein said metal substrate has a thickness equal to or less than 0.5 mm. 5 . (canceled) 6 . The method according to claim 1 wherein the applied anodic current density is between 5 and 10 A/dm 2 . 7 . The method according to claim 6 wherein the application time of the anodic current density is between 2 and 10 minutes. 8 . The method according to claim 1 wherein the weight concentration of said electrolyte is between 15-30%. 9 . The method according to claim 1 wherein the metal substrate is nickel or nickel alloy comprising a further step (c) subsequent to step (b) of nickel electrodeposition comprising the addition to said electrolyte of a nickel salt in a concentration by weight between 150 and 300 g/l and subsequent application of a cathodic current density to said metal substrate between 0.1 and 3 A/dm 2 for a time between 0.5 and 120 minutes at a temperature between 15 and 70° C. 10 . A method for manufacturing an electrode for gas evolution in electrochemical processes, comprising the following steps: treating a metal substrate with the method of claim 1 , and applying a catalytic coating comprising one or more noble or alloy metals or their oxides and/or one or more metals belonging to the rare earth group or their oxides, to said treated metal substrate. 11 . An electrode for gas evolution in electrochemical processes comprising a metal substrate, selected from nickel or nickel alloy, prepared according to the method described in claim 1 , said metal substrate having a degree of homogeneity of the roughness profile, expressed as the mean square deviation Ra values, of less than 25%, and a catalytic coating comprising one or more noble or alloy metals or their oxides and/or one or more metals belonging to the rare earth group or their oxides. 12 . (canceled) 13 . An electrode for gas evolution in electrochemical processes comprising a metal substrate, selected from nickel or nickel alloy, prepared according to the method described in claim 9 , comprising a layer of nickel electrodeposited directly on the metal substrate and a catalytic coating comprising one or more metals or alloys or their oxides and/or one or more metals belonging to the group of rare earths or their oxides. 14 . A cell for the electrolysis of water or for the electrolysis of alkali chloride solutions comprising an anodic compartment and a cathodic compartment separated by an ion-exchange membrane or by a diaphragm, wherein the cathodic compartment is equipped with an electrode according to claim 11 .
Metal or alloy · CPC title
perforated or foraminous · CPC title
with diaphragms · CPC title
characterised by the deposition of metallic material · 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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