Method and facility for producing high-strength galavanized steel sheets
US-2017253943-A1 · Sep 7, 2017 · US
US11414736B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11414736-B2 |
| Application number | US-201816652196-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 13, 2018 |
| Priority date | Oct 26, 2017 |
| Publication date | Aug 16, 2022 |
| Grant date | Aug 16, 2022 |
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The present invention is a production method of a hot-dip galvanized steel sheet including annealing a belt-shaped steel sheet having a Si content of greater than or equal to 0.2% by mass, wherein the annealing is continuously carried out using an annealing furnace having an oxidation heating zone and a reduction heating zone in this order, while the steel sheet is fed using rollers. The annealing includes oxidizing a surface of the steel sheet in the oxidation heating zone at a temperature at which roll pickup does not occur and reducing an iron oxide layer, formed by the oxidizing, in the reduction heating zone before the iron oxide layer reaches an initial roller in the reduction heating zone.
Opening claim text (preview).
The invention claimed is: 1. A production method of a hot-dip galvanized steel sheet comprising: annealing a belt-shaped steel sheet having a Si content of greater than or equal to 0.2% by mass, wherein the annealing is carried out continuously using an annealing furnace comprising an oxidation heating zone; a conveying path under a nitrogen atmosphere, and a reduction heating zone, in this order, while the steel sheet is fed using rollers provided in each of the oxidation heating zone, the conveying path, and the reduction heating zone, and the annealing comprises: oxidizing a surface of the steel sheet in the oxidation heating zone at a temperature at which roll pickup, resulting from contact between the surface of the steel sheet and the rollers in the oxidation heating zone does not occur, and reducing an iron oxide layer, formed by the oxidizing, in the reduction heating zone before the iron oxide layer reaches an initial roller in the reduction heating zone, wherein an average thickness of the iron oxide layer formed in the oxidizing is greater than or equal to 0.1 μm and less than or equal to 1.5 μm and in the reduction heating zone, a reducing atmosphere temperature is greater than or equal to 800° C. and less than or equal to 920° C., and a distance from an inlet of the reduction heating zone to the initial roller is greater than or equal to 10 m. 2. The production method according to claim 1 , wherein an oxidation temperature of the steel sheet in the oxidizing is less than or equal to 740° C. 3. The production method according to claim 1 , wherein in the reducing, a reduction temperature of the iron oxide layer at the initial roller in the reduction heating zone is greater than or equal to 750° C., and in a segment from an inlet of the reduction heating zone to the initial roller in the reduction heating zone, a reduction time period during which the reduction temperature of the iron oxide layer is greater than or equal to 700° C. is greater than or equal to 20 sec. 4. The production method according to claim 2 , wherein in the reducing, a reduction temperature of the iron oxide layer at the initial roller in the reduction heating zone is greater than or equal to 750° C., and in a segment from an inlet of the reduction heating zone to the initial roller in the reduction heating zone, a reduction time period during which the reduction temperature of the iron oxide layer is greater than or equal to 700° C. is greater than or equal to 20 sec. 5. The production method according to claim 1 , wherein a direct-fired burner is used as a heating device for the oxidation heating zone. 6. The production method according to claim 2 , wherein a direct-fired burner is used as a heating device for the oxidation heating zone. 7. The production method according to claim 3 , wherein a direct-fired burner is used as a heating device for the oxidation heating zone. 8. The production method according to claim 4 , wherein a direct-fired burner is used as a heating device for the oxidation heating zone.
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