CN101994073B - Apparatus for producing hot dipped hot rolled steel strip - Google Patents
Apparatus for producing hot dipped hot rolled steel strip Download PDFInfo
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- CN101994073B CN101994073B CN2010105690325A CN201010569032A CN101994073B CN 101994073 B CN101994073 B CN 101994073B CN 2010105690325 A CN2010105690325 A CN 2010105690325A CN 201010569032 A CN201010569032 A CN 201010569032A CN 101994073 B CN101994073 B CN 101994073B
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- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 213
- 239000010959 steel Substances 0.000 title claims abstract description 213
- 230000009467 reduction Effects 0.000 claims abstract description 72
- 238000004519 manufacturing process Methods 0.000 claims abstract description 29
- 238000009749 continuous casting Methods 0.000 claims abstract description 28
- 238000005098 hot rolling Methods 0.000 claims abstract description 13
- 238000003618 dip coating Methods 0.000 claims abstract description 10
- 238000002791 soaking Methods 0.000 claims description 7
- 230000001590 oxidative effect Effects 0.000 claims description 4
- 238000007254 oxidation reaction Methods 0.000 abstract description 87
- 230000003647 oxidation Effects 0.000 abstract description 83
- 238000000034 method Methods 0.000 abstract description 52
- 238000005266 casting Methods 0.000 abstract description 15
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 85
- 238000005246 galvanizing Methods 0.000 description 45
- 238000007747 plating Methods 0.000 description 40
- 230000008569 process Effects 0.000 description 20
- 230000002829 reductive effect Effects 0.000 description 17
- 238000012545 processing Methods 0.000 description 14
- 150000001875 compounds Chemical class 0.000 description 13
- 238000001816 cooling Methods 0.000 description 13
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 13
- 239000010960 cold rolled steel Substances 0.000 description 12
- 238000010438 heat treatment Methods 0.000 description 12
- 239000002131 composite material Substances 0.000 description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- 238000007654 immersion Methods 0.000 description 9
- 229910052760 oxygen Inorganic materials 0.000 description 9
- 239000001301 oxygen Substances 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 8
- 238000009434 installation Methods 0.000 description 8
- 229910052814 silicon oxide Inorganic materials 0.000 description 8
- 239000003795 chemical substances by application Substances 0.000 description 6
- 239000011248 coating agent Substances 0.000 description 6
- 238000000576 coating method Methods 0.000 description 6
- 238000007598 dipping method Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 6
- 238000005096 rolling process Methods 0.000 description 6
- 229910004298 SiO 2 Inorganic materials 0.000 description 5
- 230000006866 deterioration Effects 0.000 description 5
- 238000005554 pickling Methods 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 230000033228 biological regulation Effects 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 229910052725 zinc Inorganic materials 0.000 description 4
- 239000011701 zinc Substances 0.000 description 4
- 238000000137 annealing Methods 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000002950 deficient Effects 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000003472 neutralizing effect Effects 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 2
- 229910004709 CaSi Inorganic materials 0.000 description 1
- 229910001335 Galvanized steel Inorganic materials 0.000 description 1
- 229910001374 Invar Inorganic materials 0.000 description 1
- 206010070834 Sensitisation Diseases 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000007716 flux method Methods 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 239000008397 galvanized steel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 230000008313 sensitization Effects 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/04—Ferrous alloys, e.g. steel alloys containing manganese
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
- C21D9/46—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for sheet metals
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
- C21D9/52—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
- C21D9/54—Furnaces for treating strips or wire
- C21D9/56—Continuous furnaces for strip or wire
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
- C21D9/52—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
- C21D9/54—Furnaces for treating strips or wire
- C21D9/56—Continuous furnaces for strip or wire
- C21D9/561—Continuous furnaces for strip or wire with a controlled atmosphere or vacuum
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/001—Ferrous alloys, e.g. steel alloys containing N
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/002—Ferrous alloys, e.g. steel alloys containing In, Mg, or other elements not provided for in one single group C22C38/001 - C22C38/60
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/02—Ferrous alloys, e.g. steel alloys containing silicon
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/06—Ferrous alloys, e.g. steel alloys containing aluminium
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/003—Apparatus
- C23C2/0038—Apparatus characterised by the pre-treatment chambers located immediately upstream of the bath or occurring locally before the dipping process
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/02—Pretreatment of the material to be coated, e.g. for coating on selected surface areas
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/02—Pretreatment of the material to be coated, e.g. for coating on selected surface areas
- C23C2/022—Pretreatment of the material to be coated, e.g. for coating on selected surface areas by heating
- C23C2/0222—Pretreatment of the material to be coated, e.g. for coating on selected surface areas by heating in a reactive atmosphere, e.g. oxidising or reducing atmosphere
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- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/02—Pretreatment of the material to be coated, e.g. for coating on selected surface areas
- C23C2/022—Pretreatment of the material to be coated, e.g. for coating on selected surface areas by heating
- C23C2/0224—Two or more thermal pretreatments
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/02—Pretreatment of the material to be coated, e.g. for coating on selected surface areas
- C23C2/024—Pretreatment of the material to be coated, e.g. for coating on selected surface areas by cleaning or etching
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/74—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
- C21D1/76—Adjusting the composition of the atmosphere
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D8/00—Modifying the physical properties by deformation combined with, or followed by, heat treatment
- C21D8/02—Modifying the physical properties by deformation combined with, or followed by, heat treatment during manufacturing of plates or strips
- C21D8/0278—Modifying the physical properties by deformation combined with, or followed by, heat treatment during manufacturing of plates or strips involving a particular surface treatment
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- Chemical Kinetics & Catalysis (AREA)
- Thermal Sciences (AREA)
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Abstract
本发明提供一种热浸镀热轧钢板的制造设备，其是用于将用薄板坯连铸法铸造及热轧而制造的钢板进行热浸镀的热浸镀热轧钢板的制造设备，其中，具有用于氧化的炉子和用于还原的炉子，所述用于氧化的炉子和所述用于还原的炉子在沿着所述钢板的输送方向的长度之比为0.5～0.9。
The present invention provides a manufacturing facility of a hot-dip-coated hot-rolled steel sheet, which is a manufacturing facility for hot-dip-coated hot-rolled steel sheets for hot-dip-coating a steel sheet manufactured by casting and hot-rolling a thin slab continuous casting method, wherein , having a furnace for oxidation and a furnace for reduction, the ratio of the lengths of the furnace for oxidation and the furnace for reduction along the conveying direction of the steel plate is 0.5-0.9.
Description
The application be the applying date be on March 27th, 2006, one Chinese patent application number be 200680011112.0, denomination of invention divides an application for " method of manufacture of hot-dipped hot-rolled steel sheet ".
Technical field
The present invention relates to carry out with the hot-rolled steel sheet of sheet blank continuous casting manufactured the producing apparatus of the hot-dipped hot-rolled steel sheet of hot dip process.
Background technology
In recent years, based on the necessity of save energy and cutting down cost, adopted the steel plate manufacturing technology of opening the sheet blank continuous casting method of being put down in writing in the flat 2-197358 communique (Thin Slab Casting Process) like the spy to climb up stage in the world.This sheet blank continuous casting method is characterised in that, directly gives rolling process with steel plate from continuous casting working procedure.Therefore, remove with the cooling, detection of defects, the defective that between continuous casting working procedure and rolling process, need steel billet and the continuous caster of the type in the past of multiple working procedure such as heating is compared, Energy efficiency is very high, and cost of equipment also can be suppressed at low-level.In addition, can this thinslab casting and the electric furnace that with the iron and steel scrap is raw material together be utilized, also be noticeable major cause.
But, compare with the steel plate of using continuous caster manufacturing in the past with the steel plate of sheet blank continuous casting manufactured, there is the problem that is difficult to guarantee surface quality.Therefore, the sheet blank continuous casting method does not obtain extensively popularizing yet up to date.In addition, the information of relevant hot-rolled steel sheet with the sheet blank continuous casting manufactured is also considerably less, and when this hot-rolled steel sheet was carried out galvanizing, directly employing was in the past the used method of hot-rolled steel sheet by continuous caster production.
As hot-rolled steel sheet is carried out method of hot-dip galvanizing, generally can adopt " non-oxidation furnace mode ".In the method, make hot-rolled steel sheet, carry out oxidation, reduction processing through heat continuously through non-oxidation furnace, reduction furnace (lehre) and cool furnace.Like this, after oxide treatment in non-oxidation furnace, in reduction furnace, reduce processing, can form the Fe layer on the hot-rolled steel sheet surface thus.Because the sulls such as FeO of surface of steel plate are difficult to adhesion heat immersion plating,, has raising for the infiltrating effect of the plating of hot dip process therefore through removing sull from surface of steel plate.
Above-mentioned hot-dip coating installation in the past is because being that main purpose designs through cold-rolled steel sheet, so the heat-up rate of heating zone is greatly about 10 ℃/second～20 ℃/second scope.In addition, using this hot-dip coating installation hot-rolled steel sheet to be carried out under the situation that plating handles, owing to need not carry out recrystallization annealing, so the top temperature during annealing generally is adjusted at about 640 ℃～660 ℃ for common steel.
In addition, as other method, " hot dip process method (flux method) " etc. also is known.In the method, on surface of steel plate, be coated with flux such as zinc chloride, ammonium chloride, make the surface of steel plate sensitization, to improve wellability for hot dip process.But this method does not adopt owing to the problem that is difficult to manufacturing continuously or plating adhesivity aspect has in the hot dip process steel plate is made usually.
If the hot-rolled steel sheet to adopting the sheet blank continuous casting manufactured carries out galvanizing with the hot dip process steel plate method of manufacture that adopts above-mentioned " plating equipment of non-oxidation furnace mode ", then take place not plate on the surface of galvanizing rolled sheet material.According to thinking that one of them reason is the interpolation of the distinctive Ca of sheet blank continuous casting method.
Thinslab casting is owing to compare with continuous caster in the past, and the width of casting mold is very narrow, and injection nozzle also forms special construction, therefore is easy to generate the spray nozzle clogging that is caused by aluminum oxide.Therefore, in order to prevent to stop up, in thinslab casting, in ladle, add Ca to reduce the fusing point of aluminum oxide.
In the sheet blank continuous casting method, with casting from 50mm to 80mm about slab to remain on the pyritous state, directly send into rolling process and be rolled.This hot rolls is the hot rolls that is equivalent to the finishing mill of hot-rolled process in the past, can be rolled down to the thickness about 1.2mm～4mm, thereby makes hot-rolled steel sheet.In such cases, for the thin slab insulation, adopt long tunnel furnace of residence time, the amount of the iron scale that therefore generates on the thin slab surface before rolling is many.
By adding as stated and remaining in the Ca oxidation in above-mentioned iron scale in the thin slab, with the form reservation of CaO.The result is according to thinking, makes the sull on hot-rolled steel sheet surface produce spot or pit when adding in the non-oxidation furnace of oxide compound CaO in plating process that this Ca generates oxidation, and the plating wellability when making galvanizing is deterioration partly, and it is bad to produce plating.
In addition, observe and adopt the hot-rolled steel sheet of sheet blank continuous casting manufactured to compare with continuous caster in the past, the amount of dirt increases.This be because, in the sheet blank continuous casting method, because the steel plate of casting is directly sent into rolling process and is rolled to remain on the pyritous state, so Fe
3C and C are easily with remaining with the isolating state of surface of steel plate.If a large amount of remaining these Fe on the surface of hot-rolled steel sheet
3C etc., then when oxidation in non-oxidation furnace, C and oxygen react, and the generation of the sull of Fe is partly slowed down, and on sull, produces spot or pit.According to thinking, these spots or pit also make the plating wellability reduction with zinc, and it is bad to produce plating.
Find in addition, if, then bend with the hot-rolled steel sheet of in the past heat dipping coating line manufacturing employing sheet blank continuous casting manufactured.Particularly the hot-rolled steel sheet of the thickness of slab more than the 2mm bends significantly.Its reason is because when making with heat dipping coating line in the past, in heating, annealing stage yield-point required above decline takes place, particularly because when thickness of slab be 2mm more than hot-rolled steel sheet through the time, pass through at the steel plate behind the plating that generation bends on the line.
In order to prevent bending, the steel plate that had in the past proposed after plating post-heating steel plate is adjusted the technology of yield-point or strengthened plating directly reduces the technology of bending deformation quantity through the roller of line, but before a kind of technical operation numerous and diverse.A kind of technology in back is that high-precision processing such as roll profile are being made large diameter roll, requires much skill and processing units, and the manufacturing expense of roll improves with comparing greatly in the past as a result.
Summary of the invention
The present invention proposes in view of the above problems, and its purpose is, provides a kind of when the hot-rolled steel sheet hot dip process that will use the sheet blank continuous casting manufactured, especially can prevent the method for not plating in the coating surface generation.
For addressing the above problem; According to the present invention; A kind of method of manufacture of hot-dipped hot-rolled steel sheet is provided; It comprises the steps: to make steel plate with casting of sheet blank continuous casting method and hot rolling in the steel that quality % contains 0.03% above C, 0.02% above Si, 0.15% above Mn, 0.001% above Ca; Is to heat and the time of oxide treatment more than 15 seconds more than 25 ℃/second this steel plate to be up to that to reach steel billet temperature be more than 550 ℃ and to be lower than 650 ℃, heat-up rate, is that 25 seconds～45 seconds mode heats and reduces processing to be up to that to reach steel billet temperature be 700 ℃～760 ℃, steel billet temperature in the time more than 570 ℃, carries out hot dip process then.
In addition, in the method for manufacture of above-mentioned hot-dipped hot-rolled steel sheet, also can hot dip process be defined as galvanizing.
In addition; According to the present invention, a kind of producing apparatus of hot-dipped hot-rolled steel sheet is provided, it is characterized in that: it is to be used for the casting of sheet blank continuous casting method and hot rolling and the steel plate of making carries out the producing apparatus of the hot-dipped hot-rolled steel sheet of hot dip process; It has preheating oven and non-oxidation furnace and zone of reduction; Said preheating oven and non-oxidation furnace and said zone of reduction are 0.5～0.9 at the length ratio along the throughput direction of said steel plate, and zone of reduction is made up of reduction furnace and soaking pit, or only is made up of reduction furnace.
In addition, in the producing apparatus of hot-dipped hot-rolled steel sheet of the present invention, can it be 15 seconds～25 seconds also with the time set of said steel plate through said preheating oven and non-oxidation furnace.
According to the present invention, in the time will carrying out hot dip process, can prevent that the plating that on coating surface, takes place from not going up with the steel plate of sheet blank continuous casting manufactured.In addition, hot dip process also can not take place to carry out bendingly.
Description of drawings
Fig. 1 is the pie graph of preferred galvanizing hot-rolling steel plate producing equipment of the present invention.
Fig. 2 is the diagram of the temperature variation of non-oxidation furnace and the lehre of explanation in the preferred galvanizing hot-rolling steel plate producing equipment of the present invention.
Fig. 3 is with the diagram before and after the hot-rolled steel sheet oxidation that utilizes the sheet blank continuous casting manufactured.Hot-rolled steel sheet before Fig. 3 (a) expression oxidation, Fig. 3 (b) expression utilizes the hot-rolled steel sheet after the oxidation of the present invention, and Fig. 3 (c) expression utilizes the hot-rolled steel sheet after the technological in the past oxidation.
Fig. 4 is with the diagram before and after the hot-rolled steel sheet reduction of non-oxidation furnace oxidation.Hot-rolled steel sheet before Fig. 4 (d) expression reduction, Fig. 4 (e) expression snugly reductive hot-rolled steel sheet, the insufficient hot-rolled steel sheet of Fig. 4 (f) expression reduction, the superfluous hot-rolled steel sheet of Fig. 4 (g) expression reduction.
Fig. 5 is the pie graph of the washing unit of hot-dip coating installation front.
Embodiment
Below, preferred embodiment describe of the present invention with reference to accompanying drawing.In addition, in this specification sheets and accompanying drawing, for having the same mark of element annotation that same function constitutes in fact.
In the present invention; As the hot dip process steel plate made from galvanizing hot-rolled steel sheet method of manufacture; With the hot-dip galvanized steel sheet SGHC of JIS G 3302 regulation, SGH340, SGH400, SGH440, SGH540 etc. is object, adopts with the sheet blank continuous casting method and casts, rollingly contains the steel of 0.03% above C, 0.02% above Si, 0.15% above Mn, 0.001% above Ca and the steel plate made in quality %.
If Ca is lower than 0.001%, then can not prevent spray nozzle clogging sometimes, therefore contain more than 0.001%.The interpolation of Ca is normally added CaAl, CaSi or FeCa in through the molten steel after deoxidation in system steel operation, metallic Ca carries out.
Fig. 1 is the pie graph of preferred galvanizing hot-rolling steel plate producing equipment 1 of the present invention.This galvanizing hot-rolling steel plate producing equipment by the starting point of galvanizing operation production line see the batching reel 11, be provided in above-mentioned reel 10 of reel 10, terminal point off, preheating oven (not shown go out), non-oxidation furnace 12, the lehre 15 that comprises zone of reduction 13 and cooling zone 14, Zinc Pot for Galvanizing by Dipping 16, wiping arrangement 17 and cool furnace 18 between 11 constitutes.
Seeing reel 10 off is that the hot-rolled steel sheet of direct rolling manufacturing batches the reel that forms under the situation that does not reduce temperature by cast the steel that contains 0.03% above C, 0.02% above Si, 0.15% above Mn, 0.001% above Ca in quality % with the sheet blank continuous casting method after.
The lehre 15 that sets with non-oxidation furnace 12 with being connected by be used to reduce oxidized mistake hot-rolled steel sheet zone of reduction 13 and constitute at the cooling zone 14 that is used for cooling hot-rolled steel plate thereafter, the length that is its throughput direction is for example at the stove of 70m～100m.In this embodiment because steel plate is 120m/ minute through speed, so the recovery time of hot-rolled steel sheet in lehre 15 for example reduction ratio faster the zone more than 570 ℃ be 25 seconds～45 seconds.In addition, with H
2And N
2Deng as the atmosphere in the lehre 15.In addition, mainly carry out reductive zone of reduction 13 and be made up of reduction furnace and soaking pit, or only be made up of reduction furnace, the length of its throughput direction for example is set in 50m～70m.
Zinc Pot for Galvanizing by Dipping 16 is the grooves that are used for heat of immersion rolled steel plate and adhesion heat immersion plating.Wiping arrangement 17 is the devices that will blow down attached to the molten metal of the surplus on the hot-rolled steel sheet through gas.Cool furnace 18 is to be used for the stove of cooling hot-rolled steel plate thereafter.
Below, adopt Fig. 2～Fig. 4 that the galvanizing hot-rolled steel sheet method of manufacture of the producing apparatus 1 that has adopted above-mentioned galvanizing hot-rolled steel sheet is described.
The diagram of the temperature variation of the surface of steel plate when Fig. 2 is the non-oxidation furnace 12 of expression hot-rolled steel sheet through galvanizing hot-rolling steel plate producing equipment 1, zone of reduction 13 and cooling zone 14.In Fig. 2; The temperature spot that hot-rolled steel sheet gets into non-oxidation furnace 12 is O; The temperature spot that withdraws from from non-oxidation furnace 12 is P, and the temperature spot that gets into the reduction furnace of zone of reduction 13 is Q, withdraws from and the temperature spot that gets into the soaking pit of zone of reduction 13 is S from the reduction furnace of zone of reduction 13; Withdraw from and the temperature spot that gets into cooling zone 14 is T from the soaking pit of zone of reduction 13, the temperature spot that withdraws from from cooling zone 14 in addition is V.
At first, see off from seeing reel 10 off, on the immersion plating line, advance, get in the non-oxidation furnace 12 via preheating oven with the hot-rolled steel sheet of sheet blank continuous casting manufactured.
Shown in the interval I of Fig. 2; Reach steel billet temperature and reach more than 550 ℃ and be lower than 600 ℃ mode to be up to, the hot-rolled steel sheets that will get in the non-oxidation furnace 12 with the heat-up rate more than 25 ℃/second heat the surface with the oxide treatment hot-rolled steel sheet with 15 seconds～25 seconds time.Here, the time of so-called oxide treatment is the time through preheating zone and non-oxidation furnace.
Fig. 3 illustrates the hot-rolled steel sheet surface before and after this oxide treatment.Hot-rolled steel sheet before Fig. 3 (a) expression oxidation, the hot-rolled steel sheet after the oxidation is carried out in Fig. 3 (b) expression according to the present invention, and in addition, Fig. 3 (c) expression is carried out the hot-rolled steel sheet after the oxidation according to technology in the past.
Through will being set at the heat-up rate of the interval I of Fig. 2 than above-mentioned heat-up rate in the past faster more than 25 ℃/second, thereby can be prevented the effect of not plating takes place.Relative therewith, be lower than 25 ℃/second if will be set in, then owing to adding the oxide compound CaO that Ca generates and the Fe of calcium-aluminate and dirt at the heat-up rate of the interval I of Fig. 2
3C etc. are former thereby take place not plate.Below, explain through heat-up rate being set in more than 25 ℃/second and the reason that can prevent not plate.
Shown in Fig. 3 (a), the Fe sull on hot-rolled steel sheet surface is that the Fe atom through the Fe layer moves to the top layer, with the oxygen reaction and generate.In addition, when generating the Fe sull,, therefore under the Fe sull, generate SiO because the Si and the Mn that are present in the steel plate are also oxidized the samely with Fe
2Reach 2 sulls such as MnO.Here, when generating the Fe sull, if CaO, the Fe shown in Fig. 3 (a)
3C etc. can hinder the generation of Fe sull attached on the surface of steel plate, form the pit 19 shown in Fig. 3 (c).Be Fe
3During C, decomposed,, then shown in Fig. 3 (c), hinder the generation of Fe sull with the oxygen reaction by C.As stated, if form pit 19, shown in Fig. 3 (c), SiO appears from the teeth outwards then
2Reach 2 sulls such as MnO.Because these SiO
2And 2 sulls such as MnO make the wellability deterioration with galvanizing, so when carrying out galvanizing, take place not plate.
Therefore, in the present invention, heat-up rate is set in the high value more than 25 ℃/second, has accelerated the formation speed of Fe sull.
If the raising Heating temperature, but then owing to the generation of promotes oxidn film, so rate of heating is fast more, the formation speed of sull is also fast more.Because the generation of sull mainly is owing to Fe causes to moving of surface, so if the formation speed of sull is fast, the result can extrude CaO, Fe to surface of steel plate
3Even C etc. are because of CaO, Fe
3C etc. generate for example pit, also can form the Fe sull in the bottom.
This effect can be estimated as, and the oxygen concn on invar plate surface is high and form Fe on the extremely surface at steel plate in when heating
2O
3(rhombohedral iron ore).We can say Fe
2O
3Generation be to carry out to the inboard diffusion of steel plate through oxygen.Can think that thus the result has extruded CaO, Fe to surface of steel plate
3C etc.
Because the inner oxygen concn of the Fe sull on surface reduces more past inside from the top layer more, therefore at Fe
2O
3Downside, generating Fe below 570 ℃
3O
4(magnetite) generating FeO (w) more than 570 ℃.These Fe
3O
4Or FeO grows to external diffusion through the Fe ionic.Therefore, more than 570 ℃, generate Fe on the utmost point top layer of said steel plate
2O
3, generate Fe down at it
3O
4, generate FeO down at it again.When being lower than 570 ℃, generate Fe on utmost point top layer
2O
3, generate Fe down at it
3O
4
At these FeO or Fe
2O
3Below, 2 sulls that generate when Si in steel or Mn concentration are high that oxide compound by Si or Mn constitutes or constitute by the composite oxides of Si and Mn.
If CaO, Fe
3C etc. form the state of not extruding to the surface attached on the surface of steel plate, then because through CaO, Fe
3Oxygen is supplied with in blocking such as C from the surface, therefore at CaO or Fe
32 sulls that the following direct generation of C etc. is made up of the oxide compound of Si or Mn or is made up of the composite oxides of Si and Mn.In such cases, if in the process that ensuing reduction is handled, CaO, the Fe on surface
3C etc. come off, and will generate the pit of the state that the composite oxides of oxide compound or Si and the Mn of Si or Mn expose from the teeth outwards, and the result detects plating and do not go up behind plating.
But, as previously mentioned, under the situation that heat-up rate is set in the high value more than 25 ℃/second, because attached to CaO on the surface of steel plate or Fe
3C etc. are expressed on the surface, and the oxygen concn of the pit after therefore extruding increases, owing to generate Fe in this part
3O
4Or FeO, so can not form the state that the composite oxides of oxide compound or Si and the Mn of Si or Mn expose on the surface.
Thus, even because of receiving CaO, Fe
3The obstruction of C etc. and on the Fe sull, form the pit 19 shown in Fig. 3 (b) also can form the Fe sull in the bottom of this pit 19.Therefore, SiO
2And 2 sulls such as MnO are covered by the Fe sull, can on surface of steel plate, not expose.
That is, the proterties of the surface of steel plate when temperature-rise period finishes becomes following form: shown in Fig. 3 (b), and the Fe (steel plate) that comes into existence from the inboard, 2 sulls that constitute or constitute by the composite oxides of Si and Mn by the oxide compound of Si or Mn, above that by Fe
3O
4With FeO or the sull that constitutes by FeO, there are CaO, Fe from the teeth outwards
3C is at CaO, Fe
3Pit is arranged below the C, but have the FeO layer.
Relative therewith, be lower than 25 ℃/second if heat-up rate is set at, then because CaO, Fe
3C etc. are difficult to extrude to the surface, so shown in Fig. 3 (c), constituted or exposed from the teeth outwards by 2 sulls that the composite oxides of Si and Mn constitute by the oxide compound of Si or Mn.
In addition, in Fig. 3 (b), Fig. 3 (c), the oxide compound by Si or Mn on the Fe (steel plate) is constituted or is simplified shown as " SiO by 2 sulls that the composite oxides of Si and Mn constitute
2, MnO ".
In addition, be set in more than 550 ℃, can be generated zone of oxidation equably, and can remove CaO or the Fe that is present in sull top layer part easily through being up in the non-oxidation furnace being reached steel billet temperature
3The effect of C etc.Reach steel billet temperature and be set at and be lower than 550 ℃ if will be up to, then can not get this effect.
In addition, be set at and be lower than 600 ℃, can prevent to generate superfluous sull through being up in the non-oxidation furnace being reached steel billet temperature.Be set in more than 600 ℃ if being up in the non-oxidation furnace reached steel billet temperature, then can generate sull superfluously, remaining sull in follow-up reduction is handled.
In such cases, the time set that heat-up rate is remained on more than 25 ℃/second is more than 15 seconds.If be lower than 15 seconds, then can not get enough oxide thickness, 2 sulls that the result is made up of the oxide compound of Si or Mn or is made up of the composite oxides of Si and Mn can be by the covering of FeO film, and exposes on the surface.
Then, shown in the interval II of Fig. 2, oxidized hot-rolled steel sheet enters into the zone of reduction 13 in the lehre 15 along advancing on the immersion plating line.In lehre 15, at first, so that be up to and reach steel billet temperature and reach 700 ℃～760 ℃, then, enter into cooling zone 14 to cool off in zone of reduction 13 heating.In the zone of reduction 13 and cooling zone 14 of hot-rolled steel sheet in lehre, steel billet temperature is remained on state reduction 25 seconds～45 seconds the time of processing more than 570 ℃.That is, in Fig. 2, from steel billet temperature be 570 ℃ temperature spot R to time of temperature spot U be set at 25 seconds～45 seconds.
The reduction treatment temperature is limited to the reasons are as follows of temperature province more than 570 ℃ here.That is, more than 570 ℃, FeO becomes the main body of ferriferous oxide, is reduced; And when being lower than 570 ℃, Fe
3O
4Become the main body of ferriferous oxide, be reduced.FeO and Fe
3O
4Compare, treatment temp is also high sometimes, thus reduction easily.Therefore this is to handle Fe because FeO is handled in reduction than reduction
3O
4Control more easily.
Above-mentioned reduction has been shown in Fig. 4 has handled the hot-rolled steel sheet surface of front and back.Hot-rolled steel sheet before reduction is handled is (d), and the hot-rolled steel sheet that the snugly reduction is handled is (e), and it is (f) that inadequate hot-rolled steel sheet is handled in reduction, and it is (g) that superfluous hot-rolled steel sheet is handled in reduction.In addition, in Fig. 4, not shownly go out CaO and Fe shown in Figure 3
3C, this be because, these CaO and Fe
3C is through lehre 13 grades the time, through reducing atmosphere H
2And N
2Deng flow and blown from surface of steel plate and fly.
In addition, in Fig. 4, will be formed at also that the oxide compound by Si or Mn on the Fe (steel plate) constitutes or be simplified shown as " SiO by 2 sulls that the composite oxides of Si and Mn constitute
2, MnO ".
The result; The sull of the form of Fig. 3 (b) is become following form by the appropriateness reduction: shown in Fig. 4 (e); 2 sulls that coming into existence Fe (steel plate) from the inboard, constitutes or constitute by the composite oxides of Si and Mn by the oxide compound of Si or Mn; Have the film that is made up of Fe above that, remaining from the teeth outwards have CaO, a Fe
3The pit of C, but under it, have the Fe layer.
Through to be up to the mode that steel billet temperature reaches 700 ℃～760 ℃ that reaches; Steel billet temperature is remained under the state more than 570 ℃ the time of the hot-rolled steel sheet reduction being handled 25 seconds～45 seconds, thereby the surface of the hot-rolled steel sheet shown in Fig. 4 (d) can be reduced by snugly in lehre 15.
That is, shown in Fig. 4 (e), the Fe sull that is generated by No oxided film is reduced processing, thereby becomes the Fe layer fully.In addition, this Fe layer also is covered with the SiO that generates through oxide treatment and reduction processing etc. fully
2Reach 2 sulls such as MnO.Owing to make SiO with the plating wellability deterioration of galvanizing
2And 2 sulls such as MnO are capped fully, so the plating wellability becomes very good, can not take place not plate.
Relative therewith, be up to when reaching steel billet temperature and being lower than 700 ℃ or time more than 570 ℃ that steel billet temperature remained on when being lower than 25 seconds, the reduction in lehre 15 is insufficient, shown in Fig. 4 (f), remaining Fe sull.Therefore, because this Fe sull makes the plating wellability deterioration for hot dip process, so take place not plate.
In addition, be up to when reaching steel billet temperature and surpassing 760 ℃ or time more than 570 ℃ that steel billet temperature remained on when surpassing 45 seconds, the reduction surplus lehre 15 in.In such cases, shown in Fig. 4 (g), the Fe sull is formed the Fe layer by fully reduction processing.But, because the oxidizing power of Si and Mn is stronger than Fe, so when the Fe sull is reduced in lehre 15, SiO
2The secondary oxidation layer that reaches MnO is grown also superfluously, exposes at surface of steel plate.As previously mentioned, because SiO
2Reach the plating wellability deterioration that MnO makes steel plate, thereby take place not plate.
Then, the hot-rolled steel sheet that is reduced 15 marches to the Zinc Pot for Galvanizing by Dipping 16 that is heated to specified temperature along the immersion plating line from lehre, is immersed in wherein, and adheres to galvanizing.
Then, adhered to the hot-rolled steel sheet of galvanizing and on the immersion plating line, advanced, the galvanizing adhesion amount on the hot-rolled steel sheet has been adjusted to specified amount with wiping arrangement 17.
Then, hot-rolled steel sheet is advanced on the immersion plating line, in cool furnace 18, is cooled.
In above embodiment; Because to be up to the mode that steel billet temperature reaches more than the 550C and is lower than 600 ℃ that reaches; By heat-up rate more than 25 ℃/second in 15 seconds～25 seconds time; The hot-rolled steel sheet that enters in the non-oxidation furnace 12 is carried out the heated oxide processing, therefore when generating the Fe sull, even because Fe
3Dirt such as C and Ca are oxide compound and produce pit 19, and the bottom of this pit 19 also can use the Fe sull to cover.
In addition; In above embodiment; Because to be up to the mode that steel billet temperature reaches 700 ℃～760 ℃ that reaches; Steel billet temperature being remained on state more than 570 ℃ in 25 seconds～45 seconds time, the hot-rolled steel sheet of oxidized mistake is heated and reduces processing, therefore can be with the Fe sull snugly reduction on hot-rolled steel sheet surface.In addition, SiO
2And 2 sulls of MnO do not expose from the teeth outwards yet.Therefore, can prevent the generation of not plating.
In addition, in above embodiment, the length setting of throughput direction of stove (preheating oven and non-oxidation furnace 12) that will be used for oxidation is at 30m～50m, and the length setting of throughput direction that will be used for reductive stove (zone of reduction 13) is at 50m～70m.Through experiment showed, that be 0.5～0.9 o'clock with being used for the reductive stove at the length ratio along the throughput direction of hot-rolled steel sheet at the stove that is used for oxidation, can obtain good plating state.In this embodiment, the stove through will being used for oxidation be used for the reductive stove and set so that reach 0.5～0.9 at length ratio along the throughput direction of hot-rolled steel sheet, can prevent the generation of not plating.In addition and since the stove that is used for oxidation be used for the reductive stove and be set to both to exceed and also do not have insufficient suitable length, so the investment of equipment cost is able to suitableization.
More than, with reference to description of drawings preferred embodiment of the present invention, but the present invention is not limited to these examples.So long as persons skilled in the art, just can know clearly and in the category of the described technical conceive of claims, can expect various modifications or revise example, and know these modifications or revise example and also belong to technical scope of the present invention certainly.
In addition, in the above-described embodiment, see hot-rolled steel sheet off, but also can directly be connected with the production line that carries out sheet blank continuous casting from seeing reel off.
In addition, in the above-described embodiment, hot-rolled steel sheet is by being passed out to non-oxidation furnace from seeing reel off, but also can carry out the carrying out washing treatment etc. on pickling and surface passing out to the non-oxidation furnace trip.
In addition, in this above-mentioned embodiment, see hot-rolled steel sheet off to non-oxidation furnace and carry out oxidation, but also can before oxidation, be provided for carrying out the device that the carrying out washing treatment etc. on pickling and surface is handled from seeing reel off.
In addition, in the above-described embodiment, adopted the lehre that comprises zone of reduction and cooling zone, but also can be as reduction furnace and cool furnace etc. adopt the single stove that separates.
In addition, in above-mentioned present embodiment, adopt galvanizing by dipping, but beyond dezincifying, also can adopt aluminium, lead, tin etc. as hot-dip.
In addition, in the above-described embodiment, the present invention has especially brought into play effect to hot-rolled steel sheet.Its reason can be estimated as, and is that crystal boundary is thick, surface-area is big because the surface of hot-rolled steel sheet is compared with the surface of cold-rolled steel sheet, oxidation and reduction is easy, the fast growth of zone of oxidation.
Here; For the amount of oxidation under the galvanizing condition that compares cold-rolled steel sheet reaches also commercial weight; To under oxidation of the present invention, reductive condition, obtaining the hot-rolled steel sheet of good plating state, use amount of oxidation of inferring cold-rolled steel sheet in the past and the mode of going back commercial weight and calculate the amount of oxidation of hot-rolled steel sheet and go back commercial weight.
The mode of inferring the amount of oxidation of cold-rolled steel sheet is to infer amount of oxidation from time and these two variablees of arrival temperature of steel plate of being trapped in preheating oven and the non-oxidation furnace.The mode of inferring the also commercial weight of cold-rolled steel sheet is to infer and commercial weight from being trapped in time of reducing in the stove of handling and these two variablees of arrival temperature of steel plate.Inferring this also during commercial weight, the also commercial weight when calculating also commercial weight and the temperature of reduction furnace temperature more than 570 ℃ the time respectively and being lower than 570 ℃ is estimated as also commercial weight with both sums.Though it is not shown with the specific form of the mode of going back commercial weight to infer these amount of oxidation, can derive from experiment.
Under the preferred oxidation of the present invention regulation, reductive condition; The strand hot rolling that to cast with thinslab casting and the hot-rolled steel sheet that obtains carries out oxidation, reduction, and amount of oxidation that will this moment, also commercial weight through infer above-mentioned amount of oxidation, also the mode of commercial weight is obtained.As a result, amount of oxidation is 0.12～0.2mg/m
2About, also commercial weight is 0.2～0.35mg/m
2About.Amount of oxidation 0.1～the 0.8mg/m of these values and the sharp cold-rolled steel sheet that obtains in a like fashion
2, commercial weight 0.45～1mg/m also
2Compare and reduce.
Can infer from The above results, compare during with cold-rolled steel sheet, because oxidation rate and reduction rate are fast, so preferred amount of oxidation during with the hot-rolled steel sheet galvanizing and their the little value of value when also the calculated value of commercial weight is than cold-rolled steel sheet.
Through using the present invention when the galvanizing of hot-rolled steel sheet, and, cold-rolled steel sheet compares when using, can shorten oxidization time, recovery time.In addition, the length of carrying out oxidation or reductive stove can be shortened, the hot-dip galvanizing device miniaturized can be made.
; Front at hot-dip coating installation of the present invention; As shown in Figure 5, be provided with alkali washing unit that does not adopt electrolytic cleaning that constitutes by alkali spray cistern 20, neutralizing treatment groove 21, warm water rinse tank 22, hot air dryer 23 and the alkali scrubber that utilizes nylon brush 24.The reason that does not adopt general used electrolytic cleaning be because; When making hot-rolled steel sheet, after hot rolling, with the surface of steel plate pickling with thinslab casting and direct with it banded hot rolls; Coating rust-preventive agent; But since from pickling to the time of carrying out hot dip process be two days with interior degree, the time is short, so the glue spread of rust-preventive agent can be than common minimizing.
But, since the surface of steel plate after pickling, remaining rust-preventive agent or the Fe that also lacks than common amount
3Therefore C etc. are adopting the alkali washing unit that does not use electrolytic cleaning, to attached to lip-deep rust-preventive agent or Fe
3After C etc. clean, utilize nylon brush to carry out neutralizing treatment, thereby remove rust-preventive agent or Fe
3C etc.
Because through above-mentioned cleaning, can remove the rust-preventive agent that burns and remove with process furnace usually, thus process furnace oxidation-stabilized to surface of steel plate, thus in atmosphere, can use oxygen.Therefore, the growing amount of sull is stable, for stably preventing not plate the preferred condition of saying so.
In addition, the suitable ratio of amount of oxidation when experiment showed, that the hot-rolled steel sheet that obtains with the strand hot rolling that will use thinslab casting casting is as object and commercial weight also is about 0.4～0.55.Yet, when the cold-rolled steel sheet that adopts in the past about 0.2～1.2 value, deviation is arranged.
Confirm in addition; If adopt oxidation operation of the present invention, reduction operation; The thickness of the hot-rolled steel sheet of making even will use the direct hot rolling of the slab of thinslab casting manufacturing is as more than the 2mm; Operation behind plating even adopt common roller directly for the conveying roller of 1500mm, does not bend yet.
Its reason is estimated to be; Be because be set in 25 ℃/second through heat-up rate with oxidation operation; With reduction operation reduced in comparison with recovery time and cold-rolled steel sheet in the past; Thereby the yield-point of steel plate improves, and can below the distortion that produces elongation at yield, steel plate passed through, so can not bend.
In addition, be 90mpm～180mpm owing to adopt the common steel plate of prior art through speed, thus can adopt the present invention, new if transform hot-dip coating installation with this velocity range.The steel plate of hot-dip coating installation is about 180mpm through the upper limit of speed in the prior art.But, pass through speed hot-dip coating installation faster if can make steel plate, then also can use present technique.In addition, as long as can realize condition of the present invention, how much all right steel plate is through the lower limit of speed.
In hot-dip galvanizing device, sometimes to the favourable economically ton of stove/hour limit, in such cases, if the thickness of slab thickening, then steel plate reduces through speed, the therefore time lengthening through oxidized still, and the result, average heating speed slows down.In such cases, also can operate the part of heating process so that satisfy heat-up rate of the present invention.
Each composition with 4 kinds of hot-rolled steel sheet A, B, C and D of sheet blank continuous casting manufactured of representing with quality % has been shown in table 1.
Table 1
Various conditions and result thereof when the method for manufacture that adopts galvanizing hot-rolled steel sheet of the present invention is made the galvanizing hot-rolled steel sheet by these 4 kinds of hot-rolled steel sheets have been shown in table 2.The manufacturing of galvanizing hot-rolled steel sheet is to carry out in the following manner: 4 kinds of hot-rolled steel sheets are passed through in preheating oven, non-oxidation furnace, reduction furnace, soaking pit and cool furnace, carry out oxide treatment, reduction processing and processing under cooling, galvanizing then.
The adhesion amount of galvanizing is at 80～120g/m
2The scope of (single face).
Table 2
As shown in table 2, number 1～4th, all satisfy the embodiment of defined terms of the present invention, the surface of the galvanizing hot-rolled steel sheet of manufacturing is extraordinary plating state.
On the other hand, the numbering 5～9th shown in the table 2, a certain comparative example of unmet defined terms of the present invention, the surface of the galvanizing hot-rolled steel sheet of manufacturing is that plating is not gone up or the immersion plating defective mode of residual oxide debris etc.
Embodiment 2
In table 3, illustrated with quality % represent with 2 kinds of hot-rolled steel sheet A of sheet blank continuous casting manufactured and each composition of B.
Table 3
Various conditions and result thereof when the method for manufacture that adopts galvanizing hot-rolled steel sheet of the present invention is made the galvanizing hot-rolled steel sheet by these 2 kinds of hot-rolled steel sheets have been shown in table 4.The manufacturing of galvanizing hot-rolled steel sheet is carried out in the following manner: in preheating oven and non-oxidation furnace, carry out oxide treatment through making 2 kinds of hot-rolled steel sheets, reduce processing at zone of reduction (reduction furnace and soaking pit), carry out galvanizing then.In addition, in this experiment, preheating oven and non-oxidation furnace are equivalent to be used for the stove of oxidation, and zone of reduction is equivalent to be used for the reductive stove.
Table 4
Numbering 3 and 4 shown in the table 4 is with the length stuck-at-7m of preheating oven, the length of non-oxidation furnace is fixed on 21m, and cooling conditions is changed, and the length of adjustment zone of reduction is so that simulation ground reaches 41m and 78m.Recovery time is the value of calculating through speed from 120m/ minute steel plate.
As shown in table 4; Numbering 1 and 2 is embodiment that the length ratio of combined length and the zone of reduction of preheating oven and non-oxidation furnace satisfies the interior condition of 0.5～0.9 the scope that is in the present invention's regulation, and the surface of the galvanizing hot-rolled steel sheet of manufacturing is extraordinary plating state.
On the other hand; Numbering 3 and 4 shown in the table 4 be the length ratio of combined length and zone of reduction of preheating oven and non-oxidation furnace at 0.5～0.9 extraneous comparative example of the present invention's regulation, the surface of the galvanizing hot-rolled steel sheet of manufacturing is the not first-class plating defective mode of plating.
In addition, the present invention implements through velocity range by the steel plate shown in the foregoing description.In such cases, steel plate is about 180mpm in existing technology through the upper limit of speed.But, pass through speed hot-dip coating installation faster if can make steel plate, also can use present technique.
In addition, as long as can realize condition of the present invention, how much all right steel plate is through the lower limit of speed.Because is 90mpm～180mpm by the common steel plate of existing technology through speed, so in hot-dip galvanizing device, sometimes to the favourable economically ton of stove/hour limit; Under these circumstances; If thickness of slab thickening, then steel plate reduces through speed, therefore the time lengthening through oxidized still; As a result, average heating speed slows down.In such cases, also can operate the part of heating process so that satisfy heat-up rate of the present invention.
According to the present invention, in the time will carrying out galvanizing, can prevent effectively that the plating that on coating surface, takes place from not going up with the hot-rolled steel sheet of sheet blank continuous casting manufactured.
Claims (2)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005097390 | 2005-03-30 | ||
| JP2005-097390 | 2005-03-30 |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2006800111120A Division CN101155935B (en) | 2005-03-30 | 2006-03-27 | Manufacturing method of hot-dipped hot-rolled steel sheet |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101994073A CN101994073A (en) | 2011-03-30 |
| CN101994073B true CN101994073B (en) | 2012-06-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2006800111120A Active CN101155935B (en) | 2005-03-30 | 2006-03-27 | Manufacturing method of hot-dipped hot-rolled steel sheet |
| CN2010105690325A Active CN101994073B (en) | 2005-03-30 | 2006-03-27 | Apparatus for producing hot dipped hot rolled steel strip |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2006800111120A Active CN101155935B (en) | 2005-03-30 | 2006-03-27 | Manufacturing method of hot-dipped hot-rolled steel sheet |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20080283157A1 (en) |
| JP (1) | JP4619404B2 (en) |
| CN (2) | CN101155935B (en) |
| BR (1) | BRPI0607715B1 (en) |
| WO (1) | WO2006106999A1 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2009129A1 (en) * | 2007-06-29 | 2008-12-31 | ArcelorMittal France | Process for manufacturing a galvannealed steel sheet by DFF regulation |
| DE102007061489A1 (en) * | 2007-12-20 | 2009-06-25 | Voestalpine Stahl Gmbh | Process for producing hardened hardenable steel components and hardenable steel strip therefor |
| CN103978035B (en) * | 2014-04-28 | 2016-09-07 | 雷光瑞 | The processing method of hot-rolled steel |
| CN106661657B (en) * | 2014-07-02 | 2018-11-06 | 杰富意钢铁株式会社 | The manufacturing method of high-strength hot-dip zinc-coated steel sheet |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1334757A (en) * | 1998-12-18 | 2002-02-06 | 埃维斯塔波拉里特公司 | Method for mfg. of strips of stainless steel and integrated rolling mill line |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3730758A (en) * | 1970-10-29 | 1973-05-01 | Bethlehem Steel Corp | Method of protecting ferrous strip in hot-dip processes |
| JPS60174852A (en) * | 1984-02-18 | 1985-09-09 | Kawasaki Steel Corp | Cold rolled steel sheet having composite structure and superior deep drawability |
| US5137586A (en) * | 1991-01-02 | 1992-08-11 | Klink James H | Method for continuous annealing of metal strips |
| JP3520155B2 (en) * | 1996-05-27 | 2004-04-19 | 新日本製鐵株式会社 | High-tensile alloyed hot-dip galvanized hot-rolled steel sheet for automobiles having excellent deformation resistance at high strain rates and method for producing the same |
| WO2001092593A1 (en) * | 2000-05-31 | 2001-12-06 | Kawasaki Steel Corporation | Cold-rolled steel sheet having excellent strain aging hardening properties and method for producing the same |
| JP3882679B2 (en) * | 2002-05-23 | 2007-02-21 | Ｊｆｅスチール株式会社 | Manufacturing method of high-strength hot-dip galvanized cold-rolled steel sheet with excellent deep-drawability with good plating appearance |
| JP4119804B2 (en) * | 2003-08-19 | 2008-07-16 | 新日本製鐵株式会社 | High-strength galvannealed steel sheet with excellent adhesion and method for producing the same |
-
2006
- 2006-03-27 CN CN2006800111120A patent/CN101155935B/en active Active
- 2006-03-27 CN CN2010105690325A patent/CN101994073B/en active Active
- 2006-03-27 JP JP2007511220A patent/JP4619404B2/en active Active
- 2006-03-27 US US11/887,176 patent/US20080283157A1/en not_active Abandoned
- 2006-03-27 BR BRPI0607715-3B1A patent/BRPI0607715B1/en active IP Right Grant
- 2006-03-27 WO PCT/JP2006/306987 patent/WO2006106999A1/en active Application Filing
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1334757A (en) * | 1998-12-18 | 2002-02-06 | 埃维斯塔波拉里特公司 | Method for mfg. of strips of stainless steel and integrated rolling mill line |
Also Published As
| Publication number | Publication date |
|---|---|
| US20080283157A1 (en) | 2008-11-20 |
| BRPI0607715A2 (en) | 2009-10-06 |
| WO2006106999A1 (en) | 2006-10-12 |
| JPWO2006106999A1 (en) | 2008-09-25 |
| CN101994073A (en) | 2011-03-30 |
| CN101155935B (en) | 2011-08-03 |
| JP4619404B2 (en) | 2011-01-26 |
| CN101155935A (en) | 2008-04-02 |
| BRPI0607715B1 (en) | 2014-12-16 |
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