WO2007005333A2 - Process for applying a metallic coating, an intermediate coated product, and a finish coated product - Google Patents

Process for applying a metallic coating, an intermediate coated product, and a finish coated product Download PDF

Info

Publication number
WO2007005333A2
WO2007005333A2 PCT/US2006/024532 US2006024532W WO2007005333A2 WO 2007005333 A2 WO2007005333 A2 WO 2007005333A2 US 2006024532 W US2006024532 W US 2006024532W WO 2007005333 A2 WO2007005333 A2 WO 2007005333A2
Authority
WO
WIPO (PCT)
Prior art keywords
grain
aluminum
steel sheet
hot
refining
Prior art date
Application number
PCT/US2006/024532
Other languages
French (fr)
Other versions
WO2007005333A3 (en
WO2007005333A9 (en
Inventor
Erin T. Mcdevitt
Original Assignee
Isg Technology Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Isg Technology Inc. filed Critical Isg Technology Inc.
Priority to CA002611888A priority Critical patent/CA2611888C/en
Priority to EP06813213A priority patent/EP1899492A2/en
Priority to BRPI0612601-4A priority patent/BRPI0612601A2/en
Priority to AU2006266187A priority patent/AU2006266187B2/en
Publication of WO2007005333A2 publication Critical patent/WO2007005333A2/en
Publication of WO2007005333A9 publication Critical patent/WO2007005333A9/en
Publication of WO2007005333A3 publication Critical patent/WO2007005333A3/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/04Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor characterised by the coating material
    • C23C2/06Zinc or cadmium or alloys based thereon
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/003Apparatus
    • C23C2/0038Apparatus characterised by the pre-treatment chambers located immediately upstream of the bath or occurring locally before the dipping process
    • C23C2/004Snouts
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/02Pretreatment of the material to be coated, e.g. for coating on selected surface areas
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/02Pretreatment of the material to be coated, e.g. for coating on selected surface areas
    • C23C2/024Pretreatment of the material to be coated, e.g. for coating on selected surface areas by cleaning or etching
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/14Removing excess of molten coatings; Controlling or regulating the coating thickness
    • C23C2/16Removing excess of molten coatings; Controlling or regulating the coating thickness using fluids under pressure, e.g. air knives
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/12All metal or with adjacent metals
    • Y10T428/12014All metal or with adjacent metals having metal particles
    • Y10T428/12028Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, etc.]
    • Y10T428/12063Nonparticulate metal component
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/12All metal or with adjacent metals
    • Y10T428/12493Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
    • Y10T428/12771Transition metal-base component
    • Y10T428/12785Group IIB metal-base component
    • Y10T428/12792Zn-base component
    • Y10T428/12799Next to Fe-base component [e.g., galvanized]

Definitions

  • the present invention is directed to a pre-treatment process for applying a grain refining particulate compound to one surface of a steel sheet prior to immersing the steel sheet in an zinc-aluminum hot-dip coating bath, it is directed to an intermediate coated product produced by the pre-treatment process, and it is directed to a finished hot-dip coated steel sheet product with a spangle free coating applied to one surface and a conventional coating applied to the opposite surface of the steel sheet.
  • spangle free refers to a spangle facet size that is not visible to the naked eye, i.e. about 0.4 mm to 0.3 mm and smaller.
  • a conventional aluminum-zinc melt used to hot-dip steel sheet can contain between 25% to 70% aluminum by weight. In the instance where the melt is Galvalume, it contains about 55% aluminum, 1.6% silicon, and a balance of zinc by weight.
  • Replacing a bath added melt with fresh melt is both expensive and dangerous to workers, and bailing the pot increases the risk of equipment damage.
  • pot inductors maintain the bath temperature at a predetermined temperature, about 440° to 460 0 C (824° to 860 0 F) during hot-dip coating. If bailing causes the level of the melt to fall below the inductors, the melt can freeze and damage the inductors. The thermal cycling can also damage the refractory lining of the pot.
  • the past practice of doping the hot-dip pot with a grain refiner compound is a less efficient practice because the grain refining particles are suspended throughout the molten aluminum-zinc coating on the steel substrate and the melt. Some of these particles become entrained in the oxide floating on the surface of the hot-dip bath where they are skimmed out of the bath. Other particles can nucleate undesirable dross particles within the bath and sink to the bottom of the pot. In both cases these particles are not available to grain refine the coating.
  • the grain refining particles that are floating on the surface of the molten aluminum-zinc coating can cause undesirable surface defects whereas grain refining particles applied directly to the steel substrate surface are unlikely to contribute to poor surface appearance.
  • the present invention includes applying a grain refining substance to at least one surface of a steel sheet, bonding the grain refining substance to the steel sheet surface, and immersing the steel sheet in an aluminum-zihc hot-dip coating bath.
  • Figure 1 is a schematic view showing a pre-treatment process that applies grain-refining particles to a steel sheet being reduced in a rolling mill.
  • Figure 2 is a schematic view showing a pre-treatment process that applies a liquid mixture containing grain-refining particles to a steel sheet in a hot-dip coating line.
  • Figure 3 is a schematic view showing a pre-treatment process that uses a fluidized bed to apply grain-refining particles to a steel sheet in a hot-dip coating line.
  • Figure 4 is a schematic view showing a pre-treatment process that uses a brush or roll apparatus to apply grain-refining particles to a steel sheet in a hot-dip coating line.
  • Figure 1 shows the preferred pre-treatment process of the present invention applying grain-refining particles to steel sheet being rolled in a cold-reduction mill.
  • Cold-reduction is a process that reduces the thickness of steel sheet in a series of passes through a single-stand reversing mill, or a series of continuous passes through an arrangement of spaced apart mill stands in a tandem mill.'
  • the reduction of the steel sheet thickness at high speed generates considerable heat and raises the temperature of both the sheet and the work rolls.
  • the generated heat is usually dissipated with a flood lubrication system that directs a rolling solution that may include, for example, tallow based or synthetic oil, a mixture of oils, or a detergent in small streams or jets against the rolls and steel sheet surface.
  • a flood lubrication system that directs a rolling solution that may include, for example, tallow based or synthetic oil, a mixture of oils, or a detergent in small streams or jets against the rolls and steel sheet surface.
  • Flood lubrication systems are able to maintain the work temperature of the steel sheet at about 65° to 120 0 C (150° to 25O 0 F).
  • Figure 1 shows the last, or exit mill stand 1 in an exemplary tandem cold-reduction mill 2 that includes multiple mill stand arrangements.
  • the steel sheet 3 receives a last reduction as it passes between work rolls 4 in the last mill stand 1, and the full-hard cold rolled steel sheet product 5 is fed onto a reel 6 where it is coiled and wrapped for shipping to a customer and/or
  • the mill stand lubrication system 7 includes a reservoir 8 that contains a mixture of oil or detergent solution 9 and grain refining particles 10.
  • the grain refining particles have a particle size range of about 0.01 and about 25 microns.
  • the liquid mixture is directed against the work rolls 4 and the steel sheet 3 to reduce work temperature and distribute the grain refining particles 10 across the width of the steel sheet before its final pass between work rolls 4. Pressure exerted by the last set of work rolls 4 mechanically bonds the distributed particles 10 to the surface of the steel sheet during the final roll pass.
  • the intermediate coated product is fed onto the take-up reel 6 where it is coiled and wrapped for shipping to a hot-dip coating line.
  • the grain refining particulate compound constituent that is bonded to the surface of the intermediate product is boride, carbide or aluminide, as disclosed in United States Patent Nos. 6,468,674 and 6,689,489 that are incorporated herein by reference.
  • the boride compounds include titanium boride (TiBa), and aluminum boride (AIB 2 and AIB 12 ).
  • the particulate compound constituent as a carbide is titanium carbide, vanadium carbide, tungsten carbide, and iron carbide, and the aluminide is titanium aluminide (TiAb) and iron aluminide.
  • the particulate compound constituent is bonded to the intermediate product in an amount that effectively reduces spangle facet size when compared to conventional aluminum-zinc alloy coatings.
  • the effective amount is with or without elemental titanium.
  • the preferred effective amount of selected grain refining compound will reduce spangle facet size to about 0,04 to 0.03 mm and smaller so that when the intermediate coated product is hot-dipped coated, the finished coated product will have a spangle free coating on one surface and a conventional aluminum-zinc coating on the opposite surface of the coated product.
  • the effective amount of grain refiner will vary depending on which compound is selected for the intermediate coated product and depending on the desired hot-dip coating weight of the finished coated product.
  • Table A shows a range of surface concentrations for the above mentioned preferred grain refining particles that will produce a total concentration of bonded particles equivalent to the bath added compositions disclosed in the incorporated references.
  • the bonded surface concentration depends on the aim coating weight (CW) for the desired finished coated product.
  • the CW range of the finished coated product is about 30 to 300 g/m 2 having an aluminum content of between 25% to 70% Al by weight and a preferred aluminum content of 55% Al by weight for a hot-dip Galvalume coatings applied to the finished coated product.
  • the shipped coil of intermediate coated product 5 is placed on reel 11 at the entry end 12 of a hot-dip coating line 13, and the leading end of coil 5 is welded, at welding station 14, to the trailing end of the sheet steel being coated in the continuous hot-dip coating line 13.
  • the incoming intermediate coated product 5 can be spliced to the trailing end of either conventional cold rolled steel sheet that has not been, pre- treated according to the present invention, or to steel sheet that has been pre-treated according to the present invention (other intermediate coated product).
  • the spliced-in intermediate coated product 5 passes between gas-fired burners 15 housed within the chamber 16 of a direct-fired furnace.
  • the rolling oil that was applied to the intermediate coated product during cold-reduction is burned off in chamber 16 leaving behind a layer of de-oiled grain refining particles bonded to one surface of intermediate product.
  • the de-oiled intermediate coated product 5 enters an annealing furnace 18 that contains a reducing atmosphere mixture 17 of about 5% to 6% hydrogen, the balance nitrogen.
  • the temperature of the steel sheet is raised to about 760 0 C (1400 0 F) and then it is cooled in the cooling section 19 of the coating line to bath temperature, about 593 0 C (1100 0 F) for a Galvalume hot-dip bath.
  • the annealed intermediate product 5 enters the hot-dip bath 20 through snout 21 to prevent exposing it to the atmosphere, and it is immersed in bath 20 where both surfaces of the steel sheet receive a coating of molten metal (aluminum-zinc alloy).
  • the bonded grain refining particles do not contaminate or alter the hot-dip bath composition.
  • the molten metal coated steel sheet exits bath 20 between gas-wipe apparatus 22 where the molten metal coating begins to solidify.
  • finished coated product 23 has an aluminum-zinc alloy coating with a refined spangle facet size on one side of the steel sheet, and a conventional aluminum-zinc alloy coating with a larger spangle facet size on the opposite side of the steel sheet, and the finished coated product is sent downstream for additional processing and/or shipping to a customer.
  • the present invention is an improvement that satisfies a long felt need in the art.
  • a coating line is now able to produce conventional aluminum- zinc alloy coatings and refined spangle aluminum-zinc alloy coatings on demand, in the same coating bath. Bath added methods of the past failed to provide such product flexibility.
  • a first alternate embodiment of the present invention includes a particle distribution system 7a that applies the grain refining particles 10a to one surface of the steel sheet 3 separate from the rolling oil 9 applied by the mill stand lubrication system 7.
  • the grain refining particles 10a are distributed across the width of the oiled steel sheet before it makes its final pass through the mill stand work rolls 4. Pressure exerted by the work rolls mechanically bonds particles 10a to the surface of the steel sheet producing an oiled, intermediate coated product 5 with a grain refining particulate compound constituent bonded to one surface.
  • the intermediate coated product is fed onto the take-up reel 6 where it is coiled and wrapped for shipping to a hot-dip coating line.
  • a second alternate embodiment of the present invention includes apparatus 7b for applying grain-refining particles to the opposite or bottom surface of steel sheet 3.
  • grain refining particles 10b and rolling oil is applied to the bottom surface of the steel sheet 3 in, a mixture similar to the preferred embodiment, or alternatively, the grain refining particles are applied to the bottom surface of the steel sheet 3 separate from the rolling oil similar to the first alternate embodiment of the present invention.
  • pressure exerted by the last work rolls 4 mechanically bonds the distributed particles 10a to the surface of the steel sheet during the final roll pass, producing an oiled, intermediate coated product 5 having a grain refining particulate compound constituent bonded to both surfaces of the steel sheet.
  • FIG. 2 A third alternate embodiment of the present invention is shown in Figure 2.
  • the incoming full-hard cold rolled steel sheet is cleaned with solvents or the like before hot dipping, not de-oiled with gas-fired burners as shown in the Figure 1 preferred embodiment.
  • coiled sheet steel product 3a that has not yet been pre-treated according to the present invention, is placed on reel 11a at entry end 12a.
  • the sheet steel 3a enters a cleaning station 24a where the rolling oil is removed and the surface of the steel sheet is prepared for hot-dip coating.
  • the steel sheet moves into a pre-treatment station 25a where a grain refining particulate compound constituent is applied preferably to one surface, or alternatively to both surfaces of the steel sheet to produce the intermediate coated product 5a.
  • the grain refining compound particles measure between 0.01 and about 25 microns, and the particles are suspended in a liquid carrier.
  • Nozzles 26 distribute the liquid mixture 10c containing grain refining particles across the width of the steel sheet.
  • the liquid carrier may be an aqueous solution such as water with a surfactant, a volatile organic compound (VOC), or any other suitable solution with good wetting properties and that will evaporate quickly. It should be understood that although the drawing shows nozzles 26 distributing the liquid mixture 10c onto the steel sheet surface, any suitable means known in the art for applying the liquid mixture to the steel sheet surface may be used without departing from the scope of the present invention.
  • An optional squeegee roll 27 is used to meter the solution and improve the distribution of grain refining particles on the surface of the steel sheet, and rolls 28a apply pressure to mechanically bond the grain refining particles to the surface.
  • Blowers 29 vaporize the carrier before the intermediate coated product 5a enters the reducing atmosphere contained within annealing furnace 18a.
  • the annealed steel sheet 5a is cooled to bath temperature in cooling section 19a. It is immersed in the molten aluminum-zinc alloy bath 20a, exits the bath as a finished coated product between gas wiped with knives 22a.
  • the finished coated product 23a has an aluminum-zinc alloy coating with a refined spangle size on one side of the steel sheet and a conventional aluminum-zinc alloy coating, with a larger spangle size, on the opposite side of the steel sheet.
  • the finished coated steel sheet is coiled and wrapped for shipping to a customer.
  • Table B shows test results for two different concentration levels of TiB 2 particles suspended in a carrier solution.
  • the first mixture contained 0.66g of TiB 2 powder having a particle size of less than 10 microns in a solution of 20ml ethanol, and 60 ml water (Solution 1).
  • the second mixture contained 1.94g of the same TiB 2 powder in the same carrier solution (Solution 2).
  • the test panels were 0.05cm (0.0182 inch) thick annealed steel sheet, de-oiled with an alkaline cleaner, and Scotch-Brite® cleaned to prepare the surface for hot-dip coating and. improve wettability.
  • test panel 1-6 was treated with 1 ml of Solution 1
  • test panel 7-12 was treated with 1 ml of Solution 2.
  • Test panels 13 and 14 were not treated with Solutions 1 and 2; one side of each panel was lightly brushed with dry Ti B 2 particles and then rolled to mechanically bond the dry particles to the surface of the test panels 13 and 14 before hot-dip coating in the test melt described below.
  • test panels 1-12 were spread with a drawdown bar and then dried under an infrared lamp.
  • the pre-treated panels 1-14 were annealed at 76O 0 C (1400 0 F) for two minutes in a 6%H2 balance N 2 atmosphere and cooled to about 593 0 C (1100 0 F) to simulate hot-dip coating line conditions before coating.
  • the treated samples were dipped into a test melt for 4 seconds.
  • the test melt was a standard Galvalume bath having a temperature of about 593°C and a nominal composition containing 55 Al, 1.8% Si, balance Zn.
  • Untreated control panels were dipped into the test melt before and after the test panels 1-14 were coated to determine if the coating bath was contaminated by the pre-treatment grain refining particles.
  • the present pre- treatment process is able to reduce conventional aluminum-zinc spangle (about 700 to 900 microns) down to a spangle facet size that is less than 200 microns, with a preferred reduced spangle facet size range between about 50 to 500 microns (0.05 mm to 0.5 mm).
  • a coil of untreated cold rolled steel sheet 3b is fed onto the entry end 12b of the continuous hot-dip coating line 13b and is prepared for hot-dip coating at cleaning station 24b.
  • the de-oiled and prepared steel sheet enters pre-treatment station 25b where a fluidized bed 30 distributes a grain refining particulate compound constituent in the form of a powder across the width of steel sheet to produce the intermediate coated product 5b.
  • the grain refining powder has a particle size between 0.01 and about 25 microns.
  • the coated steel sheet exits fluidized bed 30 between rolls 28b that apply pressure to mechanically bond the grain refining particles to the steel sheet surface.
  • the intermediate coated product 5b is annealed in furnace 18b, and then cooled to bath temperature in cooling section 19b.
  • the cooled sheet is immersed in the molten aluminum-zinc alloy bath 20a, gas wiped with knives 22b and the finished coated product 23b, having an aluminum-zinc alloy coating with a refined spangle size on one side, and a conventional aluminum-zinc alloy coating with a larger spangle size on the opposite side, is coiled and wrapped for shipping to a customer.
  • a coil of untreated cold rolled steel sheet 3c is fed into the entry end 12c of the continuous hot-dip coating line 13c and is prepared for hot-dip coating at cleaning station 24c.
  • the de-oiled and prepared steel sheet enters the pre-treatment station 25c where the intermediate coated product 5a is produced by brushing or rolling a coating of grain refining particulate compound constituent in powder form onto the sheet steel.
  • a brush or roll 33 distributes grain-refining powder fed from a hopper 32 onto the steel surface.
  • the brushed grain refining powder has a particle size between 0.01 and about 25 microns.
  • the powder coated steel sheet passes between rolls 28c that apply pressure to mechanically bond the grain refining particles to the steel sheet surface.
  • One or both sides of the steel sheet may be coated with the grain refining powder as shown in the drawing figure, However, coating one surface of the cold rolled steel sheet with grain refiner powder is preferred.
  • the intermediate coated product 5c is annealed in furnace 18c, and the annealed intermediate coated product 5c is cooled to bath temperature in cooling section 19b.
  • the coojed sheet is immersed in the molten aluminum-zinc alloy bath 20c, gas wiped with knives 22c, and the finished coated product 23c, having an aluminum-zinc alloy coating with a refined spangle size on one side of the coated steel sheet, and a conventional aluminum-zinc alloy coating with a larger spangle size on the opposite side of the coated steel sheet, is sent downstream for further processing and/or shipping to a customer.
  • the grain refining particulate compound constituent that is mechanically bonded to the steel sheet substrate in the alternate embodiments shown in Figures 2, 3, and 4 is preferably one of the boride, carbide or aluminide compounds heretofore disclosed above.
  • Figured 2-4 show pre-treating the steel sheet 3a-3c after the incoming sheet is de-oiled and prepared for hot-dip coating at cleaning stations 24a-24c to produce intermediate coated products 5a-5c, it should be understood that such grain refining pre-treatment may be applied to conventional cold rolled steel sheet in a continuous hot-dip coating line similar to coating line 13 shown in Figure 1.
  • the grain refining particulate compound constituent would be applied to at least one surface of incoming oiled cold rolled steel sheet before the incoming sheet enters the direct-fired furnace 16 for de-oiling.
  • an invention has been disclosed in terms of preferred embodiments thereof, which fulfills each and every one of the objects of the present invention as set forth above and provides new intermediate coated product, a new and improved finished coated steel product, a method of making the coated products.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Coating With Molten Metal (AREA)

Abstract

The present invention is directed to a method of refining spangle facet size in a hot-dip coated product by applying grain-refining particles to the surface of a steel substrate before immersion into the hot-dip coating bath, to an intermediate coated steel sheet, and to a finish coated steel sheet having a different coating spangle facet size on opposite surfaces.

Description

PROCESS FOR APPLYING A METALLIC COATING,
AN INTERMEDIATE COATED PRODUCT, AND
A FINISH COATED PRODUCT
BACKGROUND OF THE INVENTION
[0001] The present invention is directed to a pre-treatment process for applying a grain refining particulate compound to one surface of a steel sheet prior to immersing the steel sheet in an zinc-aluminum hot-dip coating bath, it is directed to an intermediate coated product produced by the pre-treatment process, and it is directed to a finished hot-dip coated steel sheet product with a spangle free coating applied to one surface and a conventional coating applied to the opposite surface of the steel sheet.
[0002] In the past, grain refining particulate compounds were added to a hot-dip coating bath in effective amounts to reduce the spangle facet size of the aluminum-zinc coating applied to a steel substrate. For example, United States Patent No. 6,468,674 to Friedersdorf et at., and United States Patent No. 6,689,489 to McDevitt, disclose a process that produces a hot-dip coated product with refined spangle size. The prior "bath added" process adds particulate compound constituents to the hot-dip coating bath; the compounds selected from a group consisting of boride compounds having one of titanium and aluminum, aluminide compounds containing titanium and iron, and carbide compounds containing titanium, vanadium, tungsten, and iron. The bath added technology disclosed by the prior patents is able to reduce the spangle facet size of the aluminum-zinc hot-dip coating applied to cold-reduced steel sheet. U.S. 6,468,674 and U.S. 6,689,489 are incorporated herein in their entirety by reference.
[0003] When such grain refining compounds are added to an aluminum-zinc hot-dip coating bath, they alter spangle appearance during solidification of the coating, and depending on their concentration level in the molten coating, they will produce a solidified spangle free coating. The term spangle free as used in the present specification refers to a spangle facet size that is not visible to the naked eye, i.e. about 0.4 mm to 0.3 mm and smaller.
[0004] Bath added grain refiners have certain intrinsic problems. For example, when grain-refining compounds are added to the hot-dip coating bath, conventional aluminum- zinc coatings, and in particular Galvalume® coatings, cannot be made on the coating line until after the grain refiner is removed from the melt (bath). One possible solution to this problem is diluting the bath after the desired amount of refined spangle product is made. However, dilution requires running the coating line continuously until the concentration of grain refiner in the melt falls to a level where conventional aluminum-zinc coatings can again be made. Such manufacturing practice is not practical because it interferes with scheduling and customer demands. The dilution method is also impractical because it produces about 3,000 tons of transitional coated product where the transitional product has a coating spangle facet size that falls between the desired refined spangle size and conventional aluminum-zinc coating and/or Galvalume spangle size.
[0005] Another possible solution for overcoming the bath added grain refiner problem is bailing the molten metal from the coating pot and replacing it with fresh conventional aluminum-zinc or Galvalume melt. A conventional aluminum-zinc melt used to hot-dip steel sheet can contain between 25% to 70% aluminum by weight. In the instance where the melt is Galvalume, it contains about 55% aluminum, 1.6% silicon, and a balance of zinc by weight. Replacing a bath added melt with fresh melt is both expensive and dangerous to workers, and bailing the pot increases the risk of equipment damage. For instance, pot inductors maintain the bath temperature at a predetermined temperature, about 440° to 4600C (824° to 8600F) during hot-dip coating. If bailing causes the level of the melt to fall below the inductors, the melt can freeze and damage the inductors. The thermal cycling can also damage the refractory lining of the pot.
loooβ] Another problem associated with bath added grain refiners is excess consumption of expensive raw materials. When grain-refining compounds are added to the pot, the refining particles are applied to both sides of the immersed steel sheet. Aluminum-zinc coated steel sheet products, and in particular, Galvalume steel sheet products, are normally used in product applications that have only one exposed surface. For example, when Galvalume steel sheet is used as roofing or siding panels, one side of the coated sheet is exposed and the opposite side is hidden from view. In such material applications, there is no neeςj to refine the spangle facet size on both sides of the panel. Therefore, bath added grain refiners of the past consume twice the amount of expensive raw material as compared to a Galvalume panel with refined spangle on only one side.
[0007] In addition to excess raw material consumption, the past practice of doping the hot-dip pot with a grain refiner compound is a less efficient practice because the grain refining particles are suspended throughout the molten aluminum-zinc coating on the steel substrate and the melt. Some of these particles become entrained in the oxide floating on the surface of the hot-dip bath where they are skimmed out of the bath. Other particles can nucleate undesirable dross particles within the bath and sink to the bottom of the pot. In both cases these particles are not available to grain refine the coating. In addition, the grain refining particles that are floating on the surface of the molten aluminum-zinc coating can cause undesirable surface defects whereas grain refining particles applied directly to the steel substrate surface are unlikely to contribute to poor surface appearance.
SUMMARY OF THE INVENTION
[0008] Accordingly, it is a first object of the present invention to reduce spangle facet size in an aluminum-zinc hot-dip coated steel sheet product without adding a grain refiner substance to the coating bath.
[0009] It is another object of the present invention to improve grain refining efficiency by providing nucleation sites along the surface of an intermediate coated steel sheet product.
[0010] It is another object of the present invention to provide nucleation sites along the surface of the intermediate coated product prior to hot-dip coating in an aluminum-zinc bath.
[0011] It is still another object of the pfesent invention to provide a pre-treatment process that applies a grain refining compound to only one surface of the intermediate coated product prior to hot-dip coating in an aluminum-zinc bath.
[0012] It is another object of the present invention to mechanically bond the grain refining particles to the surface of the intermediate coated product.
[0013] It is a further object of the present invention to provide an aluminum-zinc hot dip coated steel sheet product having a spangle free aluminum-zinc coating applied to one surface and a conventional aluminum-zinc coating applied to the opposite surface of the finished coated product.
[0014] In satisfaction of the foregoing objects and advantages, the present invention includes applying a grain refining substance to at least one surface of a steel sheet, bonding the grain refining substance to the steel sheet surface, and immersing the steel sheet in an aluminum-zihc hot-dip coating bath.
BRIEF DESCRIPTION OF THE DRAWINGS
[0015] Figure 1 is a schematic view showing a pre-treatment process that applies grain-refining particles to a steel sheet being reduced in a rolling mill.
[0016] Figure 2 is a schematic view showing a pre-treatment process that applies a liquid mixture containing grain-refining particles to a steel sheet in a hot-dip coating line.
[0017] Figure 3 is a schematic view showing a pre-treatment process that uses a fluidized bed to apply grain-refining particles to a steel sheet in a hot-dip coating line. [0018] Figure 4 is a schematic view showing a pre-treatment process that uses a brush or roll apparatus to apply grain-refining particles to a steel sheet in a hot-dip coating line.
DETAILED DESCRIPTION QF THE INVENTION
10019] Referring to the drawings, Figure 1 shows the preferred pre-treatment process of the present invention applying grain-refining particles to steel sheet being rolled in a cold-reduction mill. Cold-reduction is a process that reduces the thickness of steel sheet in a series of passes through a single-stand reversing mill, or a series of continuous passes through an arrangement of spaced apart mill stands in a tandem mill.' During cold rolling, the reduction of the steel sheet thickness at high speed generates considerable heat and raises the temperature of both the sheet and the work rolls. The generated heat is usually dissipated with a flood lubrication system that directs a rolling solution that may include, for example, tallow based or synthetic oil, a mixture of oils, or a detergent in small streams or jets against the rolls and steel sheet surface. Flood lubrication systems are able to maintain the work temperature of the steel sheet at about 65° to 1200C (150° to 25O0F). Figure 1 shows the last, or exit mill stand 1 in an exemplary tandem cold-reduction mill 2 that includes multiple mill stand arrangements. The steel sheet 3 receives a last reduction as it passes between work rolls 4 in the last mill stand 1, and the full-hard cold rolled steel sheet product 5 is fed onto a reel 6 where it is coiled and wrapped for shipping to a customer and/or storage.
[0020] The mill stand lubrication system 7 includes a reservoir 8 that contains a mixture of oil or detergent solution 9 and grain refining particles 10. The grain refining particles have a particle size range of about 0.01 and about 25 microns. The liquid mixture is directed against the work rolls 4 and the steel sheet 3 to reduce work temperature and distribute the grain refining particles 10 across the width of the steel sheet before its final pass between work rolls 4. Pressure exerted by the last set of work rolls 4 mechanically bonds the distributed particles 10 to the surface of the steel sheet during the final roll pass. This produces an intermediate coated product 5 with a grain refining particulate compound constituent bonded to one surface of the steel sheet. The intermediate coated product is fed onto the take-up reel 6 where it is coiled and wrapped for shipping to a hot-dip coating line.
[0021] In the instance where the intermediate coated product 5 is delivered to a hot- dip coating line for immersion into a molten aluminum-zinc alloy coating bath, the grain refining particulate compound constituent that is bonded to the surface of the intermediate product is boride, carbide or aluminide, as disclosed in United States Patent Nos. 6,468,674 and 6,689,489 that are incorporated herein by reference. Preferably, the boride compounds include titanium boride (TiBa), and aluminum boride (AIB2 and AIB12). The particulate compound constituent as a carbide is titanium carbide, vanadium carbide, tungsten carbide, and iron carbide, and the aluminide is titanium aluminide (TiAb) and iron aluminide. The particulate compound constituent is bonded to the intermediate product in an amount that effectively reduces spangle facet size when compared to conventional aluminum-zinc alloy coatings. The effective amount is with or without elemental titanium. The preferred effective amount of selected grain refining compound will reduce spangle facet size to about 0,04 to 0.03 mm and smaller so that when the intermediate coated product is hot-dipped coated, the finished coated product will have a spangle free coating on one surface and a conventional aluminum-zinc coating on the opposite surface of the coated product. The effective amount of grain refiner will vary depending on which compound is selected for the intermediate coated product and depending on the desired hot-dip coating weight of the finished coated product.
[0022] Table A shows a range of surface concentrations for the above mentioned preferred grain refining particles that will produce a total concentration of bonded particles equivalent to the bath added compositions disclosed in the incorporated references. The bonded surface concentration depends on the aim coating weight (CW) for the desired finished coated product.
[0023] Table A
Figure imgf000007_0001
Coating weight (CW) measured in g/m
[0024] The CW range of the finished coated product is about 30 to 300 g/m2 having an aluminum content of between 25% to 70% Al by weight and a preferred aluminum content of 55% Al by weight for a hot-dip Galvalume coatings applied to the finished coated product.
[0025] The shipped coil of intermediate coated product 5 is placed on reel 11 at the entry end 12 of a hot-dip coating line 13, and the leading end of coil 5 is welded, at welding station 14, to the trailing end of the sheet steel being coated in the continuous hot-dip coating line 13. The incoming intermediate coated product 5 can be spliced to the trailing end of either conventional cold rolled steel sheet that has not been, pre- treated according to the present invention, or to steel sheet that has been pre-treated according to the present invention (other intermediate coated product).
[0026] The spliced-in intermediate coated product 5 passes between gas-fired burners 15 housed within the chamber 16 of a direct-fired furnace. The rolling oil that was applied to the intermediate coated product during cold-reduction is burned off in chamber 16 leaving behind a layer of de-oiled grain refining particles bonded to one surface of intermediate product.
[0027] The de-oiled intermediate coated product 5 enters an annealing furnace 18 that contains a reducing atmosphere mixture 17 of about 5% to 6% hydrogen, the balance nitrogen. The temperature of the steel sheet is raised to about 7600C (14000F) and then it is cooled in the cooling section 19 of the coating line to bath temperature, about 5930C (11000F) for a Galvalume hot-dip bath. The annealed intermediate product 5 enters the hot-dip bath 20 through snout 21 to prevent exposing it to the atmosphere, and it is immersed in bath 20 where both surfaces of the steel sheet receive a coating of molten metal (aluminum-zinc alloy). Surprisingly, the bonded grain refining particles do not contaminate or alter the hot-dip bath composition. The molten metal coated steel sheet exits bath 20 between gas-wipe apparatus 22 where the molten metal coating begins to solidify. When fully solidified, finished coated product 23 has an aluminum-zinc alloy coating with a refined spangle facet size on one side of the steel sheet, and a conventional aluminum-zinc alloy coating with a larger spangle facet size on the opposite side of the steel sheet, and the finished coated product is sent downstream for additional processing and/or shipping to a customer.
[0028] Because the intermediate coated product does not contaminate the hot-dip pot with grain refining particles, the present invention is an improvement that satisfies a long felt need in the art. A coating line is now able to produce conventional aluminum- zinc alloy coatings and refined spangle aluminum-zinc alloy coatings on demand, in the same coating bath. Bath added methods of the past failed to provide such product flexibility.
[0029] Referring again to the last mill stand 1 in the tandem cold-reduction mill 2 shown in Figure 1 , a first alternate embodiment of the present invention includes a particle distribution system 7a that applies the grain refining particles 10a to one surface of the steel sheet 3 separate from the rolling oil 9 applied by the mill stand lubrication system 7. The grain refining particles 10a are distributed across the width of the oiled steel sheet before it makes its final pass through the mill stand work rolls 4. Pressure exerted by the work rolls mechanically bonds particles 10a to the surface of the steel sheet producing an oiled, intermediate coated product 5 with a grain refining particulate compound constituent bonded to one surface. The intermediate coated product is fed onto the take-up reel 6 where it is coiled and wrapped for shipping to a hot-dip coating line.
[0030] Referring again to the last mill stand in Figure 1 , a second alternate embodiment of the present invention includes apparatus 7b for applying grain-refining particles to the opposite or bottom surface of steel sheet 3. In this arrangement grain refining particles 10b and rolling oil is applied to the bottom surface of the steel sheet 3 in, a mixture similar to the preferred embodiment, or alternatively, the grain refining particles are applied to the bottom surface of the steel sheet 3 separate from the rolling oil similar to the first alternate embodiment of the present invention. In either case, pressure exerted by the last work rolls 4 mechanically bonds the distributed particles 10a to the surface of the steel sheet during the final roll pass, producing an oiled, intermediate coated product 5 having a grain refining particulate compound constituent bonded to both surfaces of the steel sheet. However, as mentioned above, except for special material applications, bonding grain-refining particles to both sides of the intermediate coated product consumes excessive amounts of grain refining material. Therefore, such an intermediate coated product is less desirable than the preferred intermediate coated product that has grain refining particles bonded to only one surface.
[0031] A third alternate embodiment of the present invention is shown in Figure 2. In certain hot-dip coating lines 13a, the incoming full-hard cold rolled steel sheet is cleaned with solvents or the like before hot dipping, not de-oiled with gas-fired burners as shown in the Figure 1 preferred embodiment. In such continuous hot-dip coating lines, coiled sheet steel product 3a, that has not yet been pre-treated according to the present invention, is placed on reel 11a at entry end 12a. The sheet steel 3a enters a cleaning station 24a where the rolling oil is removed and the surface of the steel sheet is prepared for hot-dip coating. The steel sheet moves into a pre-treatment station 25a where a grain refining particulate compound constituent is applied preferably to one surface, or alternatively to both surfaces of the steel sheet to produce the intermediate coated product 5a. The grain refining compound particles measure between 0.01 and about 25 microns, and the particles are suspended in a liquid carrier. Nozzles 26 distribute the liquid mixture 10c containing grain refining particles across the width of the steel sheet. The liquid carrier may be an aqueous solution such as water with a surfactant, a volatile organic compound (VOC), or any other suitable solution with good wetting properties and that will evaporate quickly. It should be understood that although the drawing shows nozzles 26 distributing the liquid mixture 10c onto the steel sheet surface, any suitable means known in the art for applying the liquid mixture to the steel sheet surface may be used without departing from the scope of the present invention.
[0032] An optional squeegee roll 27 is used to meter the solution and improve the distribution of grain refining particles on the surface of the steel sheet, and rolls 28a apply pressure to mechanically bond the grain refining particles to the surface. Blowers 29 vaporize the carrier before the intermediate coated product 5a enters the reducing atmosphere contained within annealing furnace 18a. The annealed steel sheet 5a is cooled to bath temperature in cooling section 19a. It is immersed in the molten aluminum-zinc alloy bath 20a, exits the bath as a finished coated product between gas wiped with knives 22a. The finished coated product 23a has an aluminum-zinc alloy coating with a refined spangle size on one side of the steel sheet and a conventional aluminum-zinc alloy coating, with a larger spangle size, on the opposite side of the steel sheet. The finished coated steel sheet is coiled and wrapped for shipping to a customer.
[0033] Table B shows test results for two different concentration levels of TiB2 particles suspended in a carrier solution. The first mixture contained 0.66g of TiB2 powder having a particle size of less than 10 microns in a solution of 20ml ethanol, and 60 ml water (Solution 1). The second mixture contained 1.94g of the same TiB2 powder in the same carrier solution (Solution 2). The test panels were 0.05cm (0.0182 inch) thick annealed steel sheet, de-oiled with an alkaline cleaner, and Scotch-Brite® cleaned to prepare the surface for hot-dip coating and. improve wettability. One side of each test panel 1-6 was treated with 1 ml of Solution 1 , and one side of each test panel 7-12 was treated with 1 ml of Solution 2. Test panels 13 and 14 were not treated with Solutions 1 and 2; one side of each panel was lightly brushed with dry Ti B2 particles and then rolled to mechanically bond the dry particles to the surface of the test panels 13 and 14 before hot-dip coating in the test melt described below.
[0034] The solutions applied to test panels 1-12 were spread with a drawdown bar and then dried under an infrared lamp. The pre-treated panels 1-14 were annealed at 76O0C (14000F) for two minutes in a 6%H2 balance N2 atmosphere and cooled to about 5930C (11000F) to simulate hot-dip coating line conditions before coating. The treated samples were dipped into a test melt for 4 seconds. The test melt was a standard Galvalume bath having a temperature of about 593°C and a nominal composition containing 55 Al, 1.8% Si, balance Zn. Untreated control panels were dipped into the test melt before and after the test panels 1-14 were coated to determine if the coating bath was contaminated by the pre-treatment grain refining particles.
[0035] Table B
Figure imgf000011_0001
Figure imgf000012_0001
Figure imgf000013_0001
[0036] Based on the above test results, it is anticipated that the present pre- treatment process is able to reduce conventional aluminum-zinc spangle (about 700 to 900 microns) down to a spangle facet size that is less than 200 microns, with a preferred reduced spangle facet size range between about 50 to 500 microns (0.05 mm to 0.5 mm).
[00371 In a fourth alternate embodiment shown in Figure 3, a coil of untreated cold rolled steel sheet 3b is fed onto the entry end 12b of the continuous hot-dip coating line 13b and is prepared for hot-dip coating at cleaning station 24b. The de-oiled and prepared steel sheet enters pre-treatment station 25b where a fluidized bed 30 distributes a grain refining particulate compound constituent in the form of a powder across the width of steel sheet to produce the intermediate coated product 5b. The grain refining powder has a particle size between 0.01 and about 25 microns. The coated steel sheet exits fluidized bed 30 between rolls 28b that apply pressure to mechanically bond the grain refining particles to the steel sheet surface. The intermediate coated product 5b is annealed in furnace 18b, and then cooled to bath temperature in cooling section 19b. The cooled sheet is immersed in the molten aluminum-zinc alloy bath 20a, gas wiped with knives 22b and the finished coated product 23b, having an aluminum-zinc alloy coating with a refined spangle size on one side, and a conventional aluminum-zinc alloy coating with a larger spangle size on the opposite side, is coiled and wrapped for shipping to a customer.
10038] Referring to Figure 4 showing a fifth alternate embodiment, a coil of untreated cold rolled steel sheet 3c is fed into the entry end 12c of the continuous hot-dip coating line 13c and is prepared for hot-dip coating at cleaning station 24c. The de-oiled and prepared steel sheet enters the pre-treatment station 25c where the intermediate coated product 5a is produced by brushing or rolling a coating of grain refining particulate compound constituent in powder form onto the sheet steel. A brush or roll 33 distributes grain-refining powder fed from a hopper 32 onto the steel surface. The brushed grain refining powder has a particle size between 0.01 and about 25 microns. The powder coated steel sheet passes between rolls 28c that apply pressure to mechanically bond the grain refining particles to the steel sheet surface. One or both sides of the steel sheet may be coated with the grain refining powder as shown in the drawing figure, However, coating one surface of the cold rolled steel sheet with grain refiner powder is preferred. The intermediate coated product 5c is annealed in furnace 18c, and the annealed intermediate coated product 5c is cooled to bath temperature in cooling section 19b. The coojed sheet is immersed in the molten aluminum-zinc alloy bath 20c, gas wiped with knives 22c, and the finished coated product 23c, having an aluminum-zinc alloy coating with a refined spangle size on one side of the coated steel sheet, and a conventional aluminum-zinc alloy coating with a larger spangle size on the opposite side of the coated steel sheet, is sent downstream for further processing and/or shipping to a customer.
[0039] The grain refining particulate compound constituent that is mechanically bonded to the steel sheet substrate in the alternate embodiments shown in Figures 2, 3, and 4 is preferably one of the boride, carbide or aluminide compounds heretofore disclosed above. In addition, although Figured 2-4 show pre-treating the steel sheet 3a-3c after the incoming sheet is de-oiled and prepared for hot-dip coating at cleaning stations 24a-24c to produce intermediate coated products 5a-5c, it should be understood that such grain refining pre-treatment may be applied to conventional cold rolled steel sheet in a continuous hot-dip coating line similar to coating line 13 shown in Figure 1. In such an alternate embodiment of the present invention, the grain refining particulate compound constituent would be applied to at least one surface of incoming oiled cold rolled steel sheet before the incoming sheet enters the direct-fired furnace 16 for de-oiling.
[0040] As such, an invention has been disclosed in terms of preferred embodiments thereof, which fulfills each and every one of the objects of the present invention as set forth above and provides new intermediate coated product, a new and improved finished coated steel product, a method of making the coated products.
[0041] Of course, various changes, modifications, and alterations from the teachings of the present invention may be contemplated by those skilled in the art without departing from the intended spirit and scope thereof. It is intended that the present invention only be limited by the terms of the appended claims.

Claims

I CLAIM:
1. A method of refining spangle facet size on a hot-dip coated steel substrate, the steps of the method comprising:
a) applying a intermediate coating of grain-refining particles to a surface of the steel substrate;
b) immersing the steel substrate into a hot-dip coating bath and applying a molten aluminum-zinc alloy coating;
c) removing the steel substrate from the hot-dip coating bath;
d) solidifying said molten aluminum-zinc alloy coating applied to the steel substrate, the intermediate coating of grain-refining particles refining spangle facet size during solidification of the molten aluminum-zinc alloy coating.
2. The method recited in claim 1 including the further step of rolling the steel substrate to mechanically bond said grain-refining particles to said surface before immersing into the hot-dip coating bath.
3. The method according to claim 1 wherein said solidified aluminum-zinc alloy coated steel substrate has a first coated surface with a refined spangle facet size and a second coated surface with a larger spangle facet size.
4. The method according to claim 3 wherein said refined spangle facet size measures less than 700 microns.
5. The method according to claim 3 wherein said refined spangle facet size measures between about 50 and 500 microns.
6. The method according to claim 3 wherein said first coated surface is spangte free.
7. The method recited in claim 1 wherein said applied grain refining particles comprise a particulate compound constituent selected from the group consisting of boride compounds having one of titanium and aluminum, aluminide compounds containing titanium and iron, and carbide compounds containing titanium, vanadium, iron, and tungsten.
8. The method recited in claim 7 wherein said particulate compound constituent is one Of TiC, TiB2, AIB2, AlB12, and TiAI3.
9. The method recited in claim 1 wherein said applied grain refining particles measure between about 0.01 microns and about 25 microns.
10. The method according to claim 1 wherein said grain refining particles are suspended in a liquid mixture applied to said surface.
11. The method according to claim 1 wherein the hot-dip coating bath contains between 25% to 70% aluminum by weight.
12. The method according to claim 1 wherein the hot-dip coating bath contains about 55% aluminurn by weight.
13. The method recited in claim 1 wherein said intermediate coating of grain-refining particles is applied to two surfaces of the steel substrate.
14. In a cold-reduction mill, a method of producing an intermediate coated product for downstream hot-dip coating in an aluminum-zinc alloy bath, the steps of the method comprising:
a) applying a coating of grain-refining particles to a surface of a steel sheet being rolled in the cold-reduction mill;
b) rolling the steel sheet to mechanically bond said grain-refining particles to the surface of said intermediate coated product.
15. The method recited in claim 14 wherein step b) includes rolling the steel sheet between work rolls in the cold-reduction mill to bond said grain-refining particles to said surface.
16. The method recited in claim 14 wherein said grain-refining particles are suspended in a rolling solution and applied to said surface.
17. The method recited in claim 14 wherein said grain-refining particles comprise a particulate compound constituent selected from the group consisting of boride compounds having one of titanium and aluminum, aluminide compounds containing titanium and iron, and carbide compounds containing titanium, vanadium, iron, and tungsten.
18. The method recited in claim 17 wherein said particulate compound constituent is one of TiC, TiB2, AIB2, AIB12, and TiAI3.
19. The method recited in claim 14 wherein said applied grain refining particles measure between about 0.01 microns and about 25 microns.
20. The method recited in claim 14 wherein said applied grain refining particles are applied to two surfaces of the steel sheet being rolled in the cold-reduction mill.
21. The method recited in claim 14 including the further steps of:
a) removing the rolling solution from said intermediate coated product;
b) immersing said intermediate coated product into a hot-dip coating bath and applying a molten aluminum-zinc alloy coating;
c) removing the aluminum-zinc alloy coated product from the hot-dip coating bath;
d) solidifying said molten aluminum-zinc alloy coating, the applied grain- refining particles refining spangle facet size during solidification.
22.. The method according to claim 21 wherein said solidified aluminum-zinc alloy coated product has a first coated surface with a refined spangle facet size and a second coated surface with a larger spangle facet size.
23. The method according to claim 22 wherein said refined spangle facet size measures less than 700 microns.
24. The method according to 22 wherein said refined spangle facet size measures between about 50 and 500 microns.
25. The method according to claim 22 wherein said first coated surface is spangle free.
26. The method according to claim 21 wherein the hot-dip coating bath contains between 25% to 70% aluminum by weight.
27. The method according to claim 21 wherein the hot-dip coating bath contains about 55% aluminum by weight.
28.An intermediate article for hot dip coating in a molten aluminum-zinc alloy coating bath, comprising: a steel sheet coated with rolling solution and having grain-refining particles mechanically bonded to a surface of said steel sheet.
29. The article of claim 28 wherein said grain-refining particles comprise a particulate compound constituent selected from the group consisting of boride compounds having one of titanium and aluminum, aluminide compounds containing titanium and iron, and carbide compounds containing titanium, vanadium, iron, and tungsten.
30. The article of claim 29 wherein said compound constituent is one of TiC, TiB2, AIB2,
Figure imgf000018_0001
31. The article of claim 28 wherein said applied grain refining particles measure between about 0.01 microns and about 25 microns,
32. The article of claim 28 wherein said applied grain refining particles are mechanically bonded to two surfaces of the steel sheet.
33. The article of claim 30 wherein said steel sheet surface contains mechanically bonded grain-refining particles in an amount ranging between about 3.23E-5 to about 0.016 g/m2 times an aim coating weight when said compound constituent is Tiβ2.
34. The article of claim 30 wherein said steel sheet surface contains mechanically bonded grain-refining particles in an amount ranging between about 2.25E-5 to about 0.011 g/m2 times an aim coating weight when said compound constituent is AIB2.
35. The article of claim 30 wherein said steel sheet surface contains mechanically bonded grain-refining particles in an amount ranging between about 1.21E-5 to about 0.006 g/m2 times an aim coating weight when said compound constituent is AIB12.
36. The article of claim 30 wherein said steel sheet surface contains mechanically bonded grain-refining particles in an amount ranging between about 2.50E-5 to about 0.0005 g/m2 times an aim coating weight when said compound constituent is TiC.
37.An aluminum-zinc alloy coated article, comprising: a steel sheet having a first coated surface with a refined spangle facet size and a second coated surface with a larger spangle facet size.
38. The article of claim 37 wherein said refined spangle facet size measures less than 700 microns.
39. The article of claim 37 wherein said refined spangle facet size measures between about 50 and 500 microns.
40. The article of claim 37 wherein said first coated surface is spangle free.
41. The article of claim 37 wherein said aluminum-zinc alloy contains 25% to 70 aluminum by weight.
42. The article of claim 37 wherein said aluminum-zinc alloy contains about 55% aluminum by weight.
PCT/US2006/024532 2005-07-01 2006-06-23 Process for applying a metallic coating, an intermediate coated product, and a finish coated product WO2007005333A2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
CA002611888A CA2611888C (en) 2005-07-01 2006-06-23 Process for applying a metallic coating, an intermediate coated product, and a finish coated product
EP06813213A EP1899492A2 (en) 2005-07-01 2006-06-23 Process for applying a metallic coating, an intermediate coated product, and a finish coated product
BRPI0612601-4A BRPI0612601A2 (en) 2005-07-01 2006-06-23 process for applying a metallic coating, an intermediate coated product, and a finished coated product
AU2006266187A AU2006266187B2 (en) 2005-07-01 2006-06-23 Process for applying a metallic coating, an intermediate coated product, and a finish coated product

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US11/174,329 US7413769B2 (en) 2005-07-01 2005-07-01 Process for applying a metallic coating, an intermediate coated product, and a finish coated product
US11/174,329 2005-07-01

Publications (3)

Publication Number Publication Date
WO2007005333A2 true WO2007005333A2 (en) 2007-01-11
WO2007005333A9 WO2007005333A9 (en) 2007-06-14
WO2007005333A3 WO2007005333A3 (en) 2007-09-20

Family

ID=37492989

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2006/024532 WO2007005333A2 (en) 2005-07-01 2006-06-23 Process for applying a metallic coating, an intermediate coated product, and a finish coated product

Country Status (7)

Country Link
US (1) US7413769B2 (en)
EP (1) EP1899492A2 (en)
AU (1) AU2006266187B2 (en)
BR (1) BRPI0612601A2 (en)
CA (1) CA2611888C (en)
TW (1) TWI316972B (en)
WO (1) WO2007005333A2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070108148A1 (en) * 2005-11-15 2007-05-17 Rubbermaid Incorporated Full hard steel storage organizer components
US20110005287A1 (en) * 2008-09-30 2011-01-13 Bibber Sr John Method for improving light gauge building materials
CN102199713B (en) * 2011-04-27 2013-01-02 大连理工大学 Long-life and anti-decay Al-Si alloy grain refiner and preparation method thereof
TWI507256B (en) * 2012-08-06 2015-11-11 China Steel Corp Production method of cold rolled products free of electrolytic cleaning
DE102013101131A1 (en) * 2013-02-05 2014-08-07 Thyssenkrupp Steel Europe Ag Apparatus for hot dip coating of metal strip
CN111270297B (en) * 2020-03-10 2021-04-13 攀钢集团攀枝花钢铁研究院有限公司 Method for reducing zinc or zinc particle defects of hot-dip galvanized sheet surface strip
CN114733738A (en) * 2022-03-24 2022-07-12 上海理工大学 Titanium alloy wire and preparation method and application thereof

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1328939A (en) * 1962-03-19 1963-06-07 Inland Steel Co Aluminum coating of a ferrous metal support
GB2110248A (en) * 1981-11-18 1983-06-15 Nisshin Steel Co Ltd Process for preparing hot-dip zinc-plated steel sheets
EP0108877A1 (en) * 1982-09-16 1984-05-23 Rabewerk Heinrich Clausing Method of applying protective coatings to the surfaces of tools and devices
JPH05247617A (en) * 1992-03-05 1993-09-24 Nippon Steel Corp Manufacture of galvannealed steel sheet having excellent powdering resistance and workability
EP0632140A1 (en) * 1993-06-29 1995-01-04 Nkk Corporation Method for producing zinc coated sheet
JP2001158953A (en) * 1999-12-03 2001-06-12 Nkk Corp HIGH-LUSTER Al-Zn ALLOY PLATED STEEL SHEET AND ITS MANUFACTURING METHOD
EP1428898A1 (en) * 2002-12-13 2004-06-16 ISG Technologies Inc. Aluminum-zinc alloy composition comprising spangle for hot-dipping steel product, method and product obtainable thereof

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2049834A (en) * 1935-12-09 1936-08-04 Flint C Elder Manufacture of hot galvanized articles
US3367753A (en) * 1965-06-22 1968-02-06 Inland Steel Co Mineral-coated, galvanized steel article
US3619247A (en) * 1968-08-29 1971-11-09 Bethlehem Steel Corp Method of producing thin, bright unspangled galvanized coatings on ferrous metal strips
BE757252A (en) * 1969-10-09 1971-03-16 British Steel Corp A process for producing a coated ferrous substrate.
US4152472A (en) * 1973-03-19 1979-05-01 Nippon Steel Corporation Galvanized ferrous article for later application of paint coating
JPS52149229A (en) * 1976-06-07 1977-12-12 Kobe Steel Ltd Surface treatment method due to fluid layer system
US4111154A (en) * 1977-04-11 1978-09-05 Heurtey Metallurgie Apparatus for the surface treatment of galvanized sheet-iron
US4568569A (en) * 1983-02-28 1986-02-04 Stein Heurtey Method and apparatus for providing composite metallic coatings on metallic strips
JP2593319B2 (en) * 1987-10-09 1997-03-26 株式会社アサヒ電子研究所 Individual search device for objects to be searched, such as files
JPH05247667A (en) 1992-03-03 1993-09-24 Mazda Motor Corp Sliding member excellent in initial fitness
FR2740145B1 (en) * 1995-10-19 1997-11-14 Lorraine Laminage SHEET COATING PROCESS
US6689489B2 (en) * 1999-10-07 2004-02-10 Isg Technologies, Inc. Composition for controlling spangle size, a coated steel product, and a coating method
JP3751879B2 (en) * 1999-10-07 2006-03-01 アイエスジー・テクノロジーズ・インコーポレイティッド COATING COMPOSITION FOR STEEL PRODUCT, COATED STEEL PRODUCT, AND STEEL PRODUCT COATING METHOD

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1328939A (en) * 1962-03-19 1963-06-07 Inland Steel Co Aluminum coating of a ferrous metal support
GB2110248A (en) * 1981-11-18 1983-06-15 Nisshin Steel Co Ltd Process for preparing hot-dip zinc-plated steel sheets
EP0108877A1 (en) * 1982-09-16 1984-05-23 Rabewerk Heinrich Clausing Method of applying protective coatings to the surfaces of tools and devices
JPH05247617A (en) * 1992-03-05 1993-09-24 Nippon Steel Corp Manufacture of galvannealed steel sheet having excellent powdering resistance and workability
EP0632140A1 (en) * 1993-06-29 1995-01-04 Nkk Corporation Method for producing zinc coated sheet
JP2001158953A (en) * 1999-12-03 2001-06-12 Nkk Corp HIGH-LUSTER Al-Zn ALLOY PLATED STEEL SHEET AND ITS MANUFACTURING METHOD
EP1428898A1 (en) * 2002-12-13 2004-06-16 ISG Technologies Inc. Aluminum-zinc alloy composition comprising spangle for hot-dipping steel product, method and product obtainable thereof

Also Published As

Publication number Publication date
US7413769B2 (en) 2008-08-19
WO2007005333A3 (en) 2007-09-20
CA2611888A1 (en) 2007-01-11
AU2006266187A1 (en) 2007-01-11
US20070003778A1 (en) 2007-01-04
CA2611888C (en) 2009-09-15
TW200706692A (en) 2007-02-16
WO2007005333A9 (en) 2007-06-14
AU2006266187B2 (en) 2010-08-05
BRPI0612601A2 (en) 2010-11-23
TWI316972B (en) 2009-11-11
EP1899492A2 (en) 2008-03-19

Similar Documents

Publication Publication Date Title
AU2006266187B2 (en) Process for applying a metallic coating, an intermediate coated product, and a finish coated product
US10550458B2 (en) Method for producing a coated metal strip having an improved appearance
AU2015390616B2 (en) Zn-Al-Mg coated steel sheet, and method of producing Zn-Al-Mg coated steel sheet
JP5208502B2 (en) Hot-dip galvanized steel sheet and method for producing the same
US20110017362A1 (en) Steel flat product having a metallic coating which protects against corrosion and method for producing a metallic zn-mg coating, which protects against corrosion, on a steel flat product
US7811674B2 (en) Hot-dip galvanizing bath and galvanized iron article
EP1472385B1 (en) Method and device for galvanizing objects
JP2015532365A (en) Method for producing metal-coated steel strip
JP5063942B2 (en) Manufacturing method of hot-dip aluminized steel sheet
JP3385970B2 (en) Manufacturing method of galvannealed steel sheet with excellent surface appearance
PL81125B1 (en) Method of producing a coated ferrous substrate[gb1269150a]
JP3387415B2 (en) Manufacturing method of galvannealed steel sheet with excellent surface appearance
CN114829666A (en) Aluminum-based alloy-plated steel sheet having excellent workability and corrosion resistance, and method for producing same
CN114761602A (en) Aluminum-based alloy-plated steel sheet having excellent workability and corrosion resistance, and method for producing same
JP3372781B2 (en) Hot-dip Zn-coated steel sheet having excellent scratch resistance and method for producing the same
BE1011059A6 (en) Method of coating a steel strip by hot dip galvanising
JP3654520B2 (en) Surface-treated steel sheet excellent in workability and corrosion resistance of machined part and method for producing the same
KR0124828B1 (en) Manufacturing method for zinc dipped steel sheet with zero-spangle
KR100812020B1 (en) Method for manufacturing continuous galvanized steel iron
JP2841898B2 (en) Alloyed hot-dip galvanized steel sheet with excellent surface smoothness
JP3275686B2 (en) Galvannealed steel sheet with excellent press formability
Jin et al. Root cause analysis of an abnormal groove-clogging failure on sink rolls in continuous hot-dip galvanizing line
JP3643559B2 (en) Surface-treated steel sheet excellent in workability and corrosion resistance of machined part and method for producing the same
PL184212B1 (en) Method of thermally treating of thin hot-dip znal coated sheets
SK286485B6 (en) Method for producing a steel strip which is provided with a zinc coating and zinc-coated steel strip

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application
ENP Entry into the national phase

Ref document number: 2611888

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 2006813213

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 2006266187

Country of ref document: AU

WWE Wipo information: entry into national phase

Ref document number: MX/a/2007/016361

Country of ref document: MX

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 2006266187

Country of ref document: AU

Date of ref document: 20060623

Kind code of ref document: A

ENP Entry into the national phase

Ref document number: PI0612601

Country of ref document: BR

Kind code of ref document: A2

Effective date: 20080102