Object processing by conversion coating
US-2017342587-A1 · Nov 30, 2017 · US
US2018363160A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018363160-A1 |
| Application number | US-201616060206-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 1, 2016 |
| Priority date | Dec 11, 2015 |
| Publication date | Dec 20, 2018 |
| Grant date | — |
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A steel sheet for cans has, on the surface thereof, in order from the steel sheet side, a chromium metal layer and a hydrous chromium oxide layer. The chromium metal layer is deposited in an amount of 50-200 mg/m 2 , and the hydrous chromium oxide layer is deposited in an amount of 3-15 mg/m 2 in terms of chromium. The chromium metal layer includes: a flat chromium metal layer that has a thickness of at least 7 nm; and a granular chromium metal layer that includes granular protrusions that are formed on the surface of the flat chromium metal layer. The maximum grain size of the granular protrusions is 150 nm or smaller. The number density of the granular protrusions per unit area is 10/μm 2 or higher.
Opening claim text (preview).
1 .- 6 . (canceled) 7 . A steel sheet for cans comprising, on a surface of a steel sheet, a chromium metal layer and a hydrated chromium oxide layer stacked in this order from a steel sheet side, wherein the chromium metal layer has a coating weight of 50 to 200 mg/m 2 , the hydrated chromium oxide layer has a coating weight of 3 to 15 mg/m 2 in terms of chromium amount, and the chromium metal layer includes: a flat chromium metal layer with a thickness of not less than 7 nm; and a granular chromium metal layer having granular protrusions formed on a surface of the flat chromium metal layer, the granular protrusions having a maximum diameter of not more than 150 nm and a number density per unit area of not less than 10 protrusions/m 2 . 8 . The steel sheet according to claim 7 , wherein the granular protrusions have a maximum diameter of not more than 100 nm. 9 . The steel sheet according to claim 7 , wherein the flat chromium metal layer has a thickness of not less than 10 nm. 10 . The steel sheet according to claim 8 , wherein the flat chromium metal layer has a thickness of not less than 10 nm. 11 . A method of manufacturing the steel sheet for cans according to claim 7 , comprising: subjecting the steel sheet to prior-stage cathodic electrolysis treatment with an aqueous solution containing a hexavalent chromium compound, a fluorine-containing compound and sulfuric acid, followed by anodic electrolysis treatment at an electric quantity density of more than 0.3 C/dm 2 but less than 5.0 C/dm 2 , and then by posterior-stage cathodic electrolysis treatment at a current density of less than 60.0 A/dm 2 and an electric quantity density of less than 30.0 C/dm 2 . 12 . The method according to claim 11 , wherein the posterior-stage cathodic electrolysis treatment is a final electrolysis treatment. 13 . The method according to claim 11 , wherein the aqueous solution used in the prior-stage cathodic electrolysis treatment, the anodic electrolysis treatment and the posterior-stage cathodic electrolysis treatment comprises only one type of aqueous solution. 14 . The method according to claim 12 , wherein the aqueous solution used in the prior-stage cathodic electrolysis treatment, the anodic electrolysis treatment and the posterior-stage cathodic electrolysis treatment comprises only one type of aqueous solution. 15 . A method of manufacturing the steel sheet for cans according to claim 8 , comprising: subjecting the steel sheet to prior-stage cathodic electrolysis treatment with an aqueous solution containing a hexavalent chromium compound, a fluorine-containing compound and sulfuric acid, followed by anodic electrolysis treatment at an electric quantity density of more than 0.3 C/dm 2 but less than 5.0 C/dm 2 , and then by posterior-stage cathodic electrolysis treatment at a current density of less than 60.0 A/dm 2 and an electric quantity density of less than 30.0 C/dm 2 . 16 . The method according to claim 15 , wherein the posterior-stage cathodic electrolysis treatment is a final electrolysis treatment. 17 . The method according to claim 15 , wherein the aqueous solution used in the prior-stage cathodic electrolysis treatment, the anodic electrolysis treatment and the posterior-stage cathodic electrolysis treatment comprises only one type of aqueous solution. 18 . The method according to claim 16 , wherein the aqueous solution used in the prior-stage cathodic electrolysis treatment, the anodic electrolysis treatment and the posterior-stage cathodic electrolysis treatment comprises only one type of aqueous solution. 19 . A method of manufacturing the steel sheet for cans according to claim 9 , comprising: subjecting the steel sheet to prior-stage cathodic electrolysis treatment with an aqueous solution containing a hexavalent chromium compound, a fluorine-containing compound and sulfuric acid, followed by anodic electrolysis treatment at an electric quantity density of more than 0.3 C/dm 2 but less than 5.0 C/dm 2 , and then by posterior-stage cathodic electrolysis treatment at a current density of less than 60.0 A/dm 2 and an electric quantity density of less than 30.0 C/dm 2 . 20 . The method according to claim 19 , wherein the posterior-stage cathodic electrolysis treatment is a final electrolysis treatment. 21 . The method according to claim 19 , wherein the aqueous solution used in the prior-stage cathodic electrolysis treatment, the anodic electrolysis treatment and the posterior-stage cathodic electrolysis treatment comprises only one type of aqueous solution. 22 . The method according to claim 20 , wherein the aqueous solution used in the prior-stage cathodic electrolysis treatment, the anodic electrolysis treatment and the posterior-stage cathodic electrolysis treatment comprises only one type of aqueous solution. 23 . A method of manufacturing the steel sheet for cans according to claim 10 , comprising: subjecting the steel sheet to prior-stage cathodic electrolysis treatment with an aqueous solution containing a hexavalent chromium compound, a fluorine-containing compound and sulfuric acid, followed by anodic electrolysis treatment at an electric quantity density of more than 0.3 C/dm 2 but less than 5.0 C/dm 2 , and then by posterior-stage cathodic electrolysis treatment at a current density of less than 60.0 A/dm 2 and an electric quantity density of less than 30.0 C/dm 2 . 24 . The method according to claim 23 , wherein the posterior-stage cathodic electrolysis treatment is a final electrolysis treatment. 25 . The method according to claim 23 , wherein the aqueous solution used in the prior-stage cathodic electrolysis treatment, the anodic electrolysis treatment and the posterior-stage cathodic electrolysis treatment comprises only one type of aqueous solution. 26 . The method according to claim 24 , wherein the aqueous solution used in the prior-stage cathodic electrolysis treatment, the anodic electrolysis treatment and the posterior-stage cathodic electrolysis treatment comprises only one type of aqueous solution.
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