WO2015129282A1 - 亜鉛系めっき鋼板およびその製造方法 - Google Patents
亜鉛系めっき鋼板およびその製造方法 Download PDFInfo
- Publication number
- WO2015129282A1 WO2015129282A1 PCT/JP2015/001053 JP2015001053W WO2015129282A1 WO 2015129282 A1 WO2015129282 A1 WO 2015129282A1 JP 2015001053 W JP2015001053 W JP 2015001053W WO 2015129282 A1 WO2015129282 A1 WO 2015129282A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- steel sheet
- oxide layer
- galvanized steel
- zinc
- alkaline aqueous
- Prior art date
Links
Images
Classifications
-
- 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
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/05—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
- C23C22/06—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
- C23C22/48—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 not containing phosphates, hexavalent chromium compounds, fluorides or complex fluorides, molybdates, tungstates, vanadates or oxalates
- C23C22/50—Treatment of iron or alloys based thereon
-
- 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
- C23C2/04—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor characterised by the coating material
- C23C2/06—Zinc or cadmium or alloys based thereon
-
- 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
- C23C2/14—Removing excess of molten coatings; Controlling or regulating the coating thickness
-
- 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
- C23C2/26—After-treatment
-
- 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
- C23C2/26—After-treatment
- C23C2/261—After-treatment in a gas atmosphere, e.g. inert or reducing atmosphere
-
- 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
- C23C2/34—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor characterised by the shape of the material to be treated
- C23C2/36—Elongated material
- C23C2/40—Plates; Strips
-
- 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
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/05—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
- C23C22/06—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
- C23C22/48—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 not containing phosphates, hexavalent chromium compounds, fluorides or complex fluorides, molybdates, tungstates, vanadates or oxalates
- C23C22/53—Treatment of zinc or alloys based thereon
-
- 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
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/05—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
- C23C22/60—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using alkaline aqueous solutions with pH greater than 8
- C23C22/62—Treatment of iron or alloys based thereon
-
- 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
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/78—Pretreatment of the material to be coated
-
- 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
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/82—After-treatment
- C23C22/83—Chemical after-treatment
-
- 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
- C23C28/00—Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
- C23C28/30—Coatings combining at least one metallic layer and at least one inorganic non-metallic layer
- C23C28/32—Coatings combining at least one metallic layer and at least one inorganic non-metallic layer including at least one pure metallic layer
- C23C28/322—Coatings combining at least one metallic layer and at least one inorganic non-metallic layer including at least one pure metallic layer only coatings of metal elements only
- C23C28/3225—Coatings combining at least one metallic layer and at least one inorganic non-metallic layer including at least one pure metallic layer only coatings of metal elements only with at least one zinc-based layer
-
- 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
- C23C28/00—Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
- C23C28/30—Coatings combining at least one metallic layer and at least one inorganic non-metallic layer
- C23C28/34—Coatings combining at least one metallic layer and at least one inorganic non-metallic layer including at least one inorganic non-metallic material layer, e.g. metal carbide, nitride, boride, silicide layer and their mixtures, enamels, phosphates and sulphates
- C23C28/345—Coatings combining at least one metallic layer and at least one inorganic non-metallic layer including at least one inorganic non-metallic material layer, e.g. metal carbide, nitride, boride, silicide layer and their mixtures, enamels, phosphates and sulphates with at least one oxide layer
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/22—Electroplating: Baths therefor from solutions of zinc
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/48—After-treatment of electroplated surfaces
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D7/00—Electroplating characterised by the article coated
- C25D7/06—Wires; Strips; Foils
- C25D7/0614—Strips or foils
Definitions
- the present invention relates to a galvanized steel sheet excellent in slidability in press molding and alkali degreasing in an automobile manufacturing process, and a method for manufacturing the same.
- galvanized steel sheet is described as including galvannealed steel sheet.
- Zinc-based galvanized steel sheets are widely used in a wide range of fields centering on automobile body applications. Zinc-based plated steel sheets for such applications are used after being subjected to press forming and painting.
- galvanized steel sheets have the disadvantage that they are inferior in press formability compared to cold-rolled steel sheets. This is because the sliding resistance of the galvanized steel sheet in the press die is larger than that of the cold-rolled steel sheet. That is, the galvanized steel sheet is less likely to flow into the press mold at a portion where the sliding resistance between the mold and the bead is large, and the steel sheet is likely to break.
- Patent Document 1 discloses that press forming properties and chemical conversion treatment properties can be achieved by forming Ni oxide on the surface of a zinc-coated steel sheet by electrolytic treatment, dipping treatment, coating oxidation treatment, or heat treatment ( A technique for improving chemical conversion (ability) is disclosed.
- Patent Documents 2 and 3 an alloyed hot-dip galvannealed steel sheet is brought into contact with a sulfuric acid solution to form an oxide layer mainly composed of Zn oxide on the surface of the steel sheet and alloyed.
- a technique for improving the slidability by suppressing adhesion between a hot-dip galvannealed coating layer and a press die is disclosed.
- Patent Document 4 discloses a technique for improving the degreasing property by washing the surface of an alloyed hot-dip galvanized steel sheet with an alkaline solution.
- Patent Document 5 discloses a technique for improving the degreasing property by washing the surface of an alloyed hot-dip galvanized steel sheet with a solution containing P.
- Patent Documents 1 to 3 the lubrication effect between the press die and the galvanized steel sheet is expressed by the lubrication effect by the contained lubricant or the like or the surface reaction layer, but the required properties are satisfied for the degreasing property. It wasn't something to do.
- Patent Documents 4 to 5 although a degreasing improvement effect is recognized, there are cases where the effect is not always sufficient under severe degreasing conditions.
- the present invention has been made in view of such circumstances, and has excellent degreasing properties even under severe alkaline degreasing conditions in which the sliding resistance during press molding is small, the temperature is low, and the line length is short.
- Another object of the present invention is to provide a zinc-based plated steel sheet and a method for producing a zinc-based plated steel sheet that can suppress the dissolution of the formed oxide layer and suppress the occurrence of unevenness due to the cleaning treatment.
- the inventors of the present invention have made extensive studies to solve the above problems.
- the oxide layer formed on the surface of the steel sheet was neutralized using an alkaline aqueous solution containing P ions at a P concentration of 0.01 g / L or more and carbonate ions at a carbonate ion concentration of 0.1 g / L or more.
- the value obtained by converting the measured oxygen strength into the thickness as the SiO 2 film is 20 nm or more (corresponding to the thickness of the oxide layer), Zn is 50 mg / m 2 or more, and S is 5 mg / m 2 or more.
- the present invention is based on the above findings, and features are as follows.
- the oxide layer includes a crystal structure represented by Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O (1) or ( 2) Zinc-based plated steel sheet.
- X is a real number of 0 ⁇ X ⁇ 1
- n is a real number of 0 ⁇ n ⁇ 10.
- the oxide layer contains at least one selected from PO 4 3 ⁇ , P 2 O 7 4 ⁇ , P 3 O 9 5 ⁇ and these inorganic acids or metal compounds,
- the galvanized steel sheet according to any one of (1) to (3), wherein the galvanized steel sheet contains at least one selected from sodium and zinc.
- the galvanized steel sheet shall be an alloyed hot dip galvanized steel sheet (hot-dip galvannealed steel sheet), hot dip galvanized steel sheet or electrogalvanized steel sheet (electrogalvanized steel sheet).
- the galvanized steel sheet according to any one of (1) to (4), which is characterized.
- the acidic solution has a pH buffering action, and the amount of 1.0 mol / L sodium hydroxide solution (L) required to raise the pH of 1 L of the acidic solution from 2.0 to 5.0.
- the acidic solution includes at least one salt selected from acetate, phthalate, citrate, succinate, lactate, tartrate, borate, and phosphate in total.
- the acidic solution adhesion amount on the steel sheet surface after contacting the acidic solution is 15 g / m 2 or less, (6) to (12), The manufacturing method of the zinc-plated steel plate as described in 1 ..
- the steel sheet is subjected to temper rolling after the zinc-based plating is performed on the steel sheet and before the oxide layer forming step.
- the sliding resistance during press molding is small, the temperature is low, and the line length is short. It is possible to obtain a zinc-based plated steel sheet that can be suppressed and the occurrence of unevenness due to the cleaning treatment can be suppressed.
- FIG. 1 is a schematic front view showing a friction coefficient measuring apparatus.
- FIG. 2 is a schematic perspective view showing the shape and dimensions of the bead used in Condition 1 of the example.
- FIG. 3 is a schematic perspective view showing the shape and dimensions of the bead used in Condition 2 of the example.
- FIG. 4 is a schematic perspective view showing the shape and dimensions of the bead used in Condition 3 of the example.
- FIG. 5 is a schematic diagram illustrating evaluation criteria for evaluating appearance unevenness.
- the method for producing a galvanized steel sheet according to the present invention comprises forming an oxide layer by bringing a galvanized steel sheet into contact with an acidic solution containing sulfuric acid ions (sulfuric acid acidic solution), holding for 1 to 60 seconds, and then washing with water. And a neutralization treatment step in which the surface of the oxide layer formed in the oxide layer forming step is kept in contact with an alkaline aqueous solution for 0.5 to 10 seconds or longer, and then washed with water and dried.
- the alkaline aqueous solution contains 0.01 g / L or more of P ions as a P concentration and 0.1 g / L or more of carbonate ions as a carbonate ion concentration.
- galvanization is performed before the oxide layer forming step.
- the method for applying zinc plating is not particularly limited, and general methods such as hot-dip galvanizing and electrogalvanizing can be employed.
- the process conditions of electrogalvanization and hot dip galvanization are not specifically limited, What is necessary is just to employ
- the additive element component in the plating bath other than Al is not particularly limited. That is, even if Pb, Sb, Si, Sn, Mg, Mn, Ni, Ti, Li, Cu or the like is contained or added in addition to Al, the effect of the present invention is not impaired.
- alloying treatment galvannealing
- the conditions for the alloying treatment are not particularly limited, and preferable conditions may be adopted as appropriate.
- the steel sheet any of those subjected to zinc plating treatment and those subjected to alloying treatment after zinc plating treatment can be used.
- the steel type of the steel sheet is not particularly limited, such as low-carbon steel (ultra-low-carbon steel), ultra-low-carbon steel (IF), IF steel, high-tensile steel sheet added with various alloy elements, etc.
- Various steel plates can be used.
- a base material steel plate either a hot-rolled steel plate or a cold-rolled steel plate can be used.
- the flat portion of the surface of the alloyed hot-dip galvanized layer is preferably 20 to 80%. If it is less than 20%, the contact area with the press die at the portion (concave portion) excluding the flat portion becomes large, and the thickness of the oxide layer to be described later is reliably controlled out of the area that actually contacts the press die. The area ratio of the flat portion that can be produced is reduced. As a result, the effect of improving press formability is reduced.
- the part except a flat part has a role which hold
- the flat part on the surface of the galvannealed layer can be easily identified by observing the surface with an optical microscope or a scanning electron microscope.
- the area ratio of the flat portion on the surface of the alloyed hot-dip galvanized layer can be determined by image analysis of the above micrograph.
- temper rolling it is preferable to perform temper rolling after the zinc-based plating and before the oxide layer forming step.
- temper rolling By applying temper rolling, surface irregularities are alleviated by planarization. As a result, at the time of press molding, the force required for the mold to crush the projections on the plating surface is reduced, and the sliding characteristics can be improved.
- the surface is activated by contacting with an alkaline aqueous solution after the zinc-based plating and before the oxide layer forming step.
- an alkaline aqueous solution used in this activation treatment is preferably in the range of pH 10-14.
- the alkaline aqueous solution used in this activation treatment preferably has a temperature in the range of 20 ° C to 70 ° C. If it is lower than 20 ° C., it may take a long time for the removal reaction of the unnecessary oxide layer, which may cause a decrease in productivity. On the other hand, when the temperature exceeds 70 ° C., the reaction proceeds relatively quickly, but seizure or uneven processing tends to occur on the steel sheet surface.
- the kind of solution is not limited, it is preferable to use chemicals, such as NaOH, from a viewpoint of cost.
- the alkaline aqueous solution may contain substances other than the elements contained in zinc-based plating such as Zn, Al, and Fe, and other components.
- the galvanized steel sheet was brought into contact with an acidic solution containing sulfuric acid (sulfuric acid is present in the acidic solution in the form of sulfate ions.
- sulfuric acid acidic solution an acidic solution containing sulfuric acid
- it is held for 1 to 60 seconds, and then washed with water to form an oxide layer on the surface of the steel sheet. Below, this oxide layer formation process is demonstrated.
- the mechanism by which the oxide layer is formed in the oxide layer forming step is not clear, it can be considered as follows.
- the dissolution of zinc causes a hydrogen generation reaction at the same time, as the dissolution of zinc proceeds, the hydrogen ion concentration in the solution decreases, and as a result, the pH of the solution rises, and the surface of the steel sheet is oxidized mainly with Zn. It is thought that a physical layer is formed.
- the acidic sulfuric acid solution used in the oxide layer forming step is not particularly limited as long as the pH is such that zinc can be dissolved to form an oxide layer (details will be described later).
- Sulfuric acid is used to adjust the pH.
- the sulfuric acid acidic solution becomes an acidic solution containing sulfate ions.
- the sulfate ion concentration in the sulfuric acid acidic solution is preferably 0.5 to 50 g / L.
- the sulfate ion concentration is less than 0.5 g / L, the amount of sulfate groups in the oxide is reduced, the amount of S in the oxide layer is less than 5 mg / m 2 , and Zn 4 (SO 4 ) 1-X ( A crystal structure represented by CO 3 ) X (OH) 6 .nH 2 O is difficult to form. If the sulfate ion concentration exceeds 100 g / L, there is no problem in quality, but this is not preferable because it leads to an increase in cost.
- a sulfuric acid acidic solution having a pH buffering action among sulfuric acid acidic solutions.
- a sulfuric acid acidic solution having a pH buffering action is less likely to instantaneously raise the pH of the solution and forms a sufficient amount of an oxide layer, compared to a sulfuric acid acidic solution having no pH buffering action.
- the oxide layer which is excellent in sliding property can be stably formed if the sulfuric acid solution to be used has a pH buffering action, the solution can contain metal ions, inorganic compounds, and the like.
- the pH buffer action of sulfuric acid acidic solution is the degree of pH increase defined by the amount (L) of 1.0 mol / L aqueous sodium hydroxide solution required to raise the pH of 1 liter acidic solution to 2.0-5.0. Can be evaluated. In the present invention, this value is preferably in the range of 0.003 to 0.5. If the degree of pH increase is less than 0.003, the pH increase may occur rapidly, so that sufficient dissolution of zinc for forming the oxide layer may not be obtained, and a sufficient amount of oxide layer may not be formed. . On the other hand, if the degree of pH increase exceeds 0.5, dissolution of zinc may be promoted too much, and it may take a long time to form an oxide layer, or damage to the plating layer may become severe.
- the role of the original rust-proof steel sheet may be lost.
- the pH increase degree of the acidic solution having a pH exceeding 2.0 is determined by adding an inorganic acid such as sulfuric acid having almost no buffering property in the pH range of 2.0 to 5.0 to the sulfuric acid acidic solution. Is once lowered to 2.0 for evaluation.
- Examples of such an acidic solution having a pH buffering action include acetates such as sodium acetate (CH 3 COONa), phthalates such as potassium hydrogen phthalate ((KOOC) C 6 H 4 (COOH)), and sodium citrate. Citrates such as (Na 3 C 6 H 5 O 7 ) and potassium dihydrogen citrate (KH 2 C 6 H 5 O 7 ), and succinates such as sodium succinate (Na 2 C 4 H 4 O 4 ) And lactate such as sodium lactate (CH 3 CHOHCO 2 Na), tartrate such as sodium tartrate (Na 2 C 4 H 4 O 6 ), borate, phosphate and the like. One or more salts selected from these are preferably contained in a total range of 5 to 50 g / L.
- the pH of the solution rises relatively quickly with the dissolution of zinc, so that an oxide layer sufficient for improving the slidability may not be formed. If it exceeds 50 g / L, dissolution of zinc is promoted, and not only does it take a long time to form an oxide layer, but also the plating layer is severely damaged, and the original role as a rust-proof steel sheet may be lost.
- the sulfuric acid acidic solution preferably has a pH of 0.5 to 5.0.
- pH is less than 0.5, dissolution of zinc is promoted, but an oxide layer is hardly formed.
- pH exceeds 5.0 the reaction rate of zinc dissolution becomes low.
- the liquid temperature of the sulfuric acid acidic solution is preferably 20 to 70 ° C. If it is lower than 20 ° C., it may take a long time for the formation reaction of the oxide layer, which may cause a decrease in productivity. On the other hand, when the temperature exceeds 70 ° C., the reaction proceeds relatively quickly, but on the contrary, processing unevenness tends to occur on the steel sheet surface.
- the method for bringing the steel sheet into contact with the sulfuric acid solution is not particularly limited.
- the amount of the sulfuric acid solution attached to the steel sheet surface after contacting with the sulfuric acid solution is preferably 15 g / m 2 or less. Moreover, 1 g / m ⁇ 2 > or more is preferable from a viewpoint of preventing drying of a liquid film.
- the amount of adhesion can be adjusted by a squeeze roll, air wiping or the like. The adhesion amount of the sulfuric acid acidic solution can be measured using a Chino Corporation infrared moisture gauge.
- the holding time until the water washing needs 1 to 60 seconds. If the time until washing with water is less than 1 second, the sulfuric acid acidic solution is washed out before the formation of the oxide layer mainly composed of Zn due to the increase in pH of the solution, so that the effect of improving the slidability cannot be obtained. . Even if it exceeds 60 seconds, no change is observed in the amount of the oxide layer.
- the holding is performed in an atmosphere containing more oxygen than the air from the viewpoint of promoting oxidation.
- the method and conditions for washing with water are not particularly limited.
- a salt having a pH buffering action present in the acidic treatment solution may inhibit the reaction with an alkaline aqueous solution containing pH 9-12 containing carbonate ions in the subsequent neutralization treatment step.
- the portion that comes into contact with the press die during press molding is preferably composed of a hard and high melting point material from the viewpoint of preventing adhesion with the press die and improving the slidability.
- the oxide layer formed in the oxide layer forming step is hard and has a high melting point. For this reason, adhesion with a press die can be prevented, and it is effective in improving sliding characteristics. In particular, good slidability can be stably obtained by performing a treatment for uniformly forming an oxide layer on the surface flat portion of the steel sheet that has been subjected to temper rolling.
- the oxide layer is abraded and scraped off by contact with the press mold, so the thickness of the oxide layer is required to the extent that the effect of the present invention is not impaired.
- the required thickness varies depending on the degree of processing by press molding. For example, in the case of processing involving large deformation or processing in which the contact area between the press die and the oxide layer is large, a thicker oxide layer is required.
- the thickness of the oxide layer may be adjusted in the range of 20 to 200 nm. By setting the average thickness of the oxide layer to 20 nm or more, a galvanized steel sheet having good slidability can be obtained. It is more effective when the thickness of the oxide layer is 25 nm or more.
- the upper limit of the thickness of the oxide layer is not particularly limited. However, when the thickness of the oxide layer exceeds 200 nm, the reactivity of the surface is extremely lowered, and it may be difficult to form a chemical conversion film. Therefore, the thickness of the oxide layer is preferably 200 nm or less. The specific thickness adjustment may be performed by appropriately changing the conditions for forming the following oxide layer.
- the surface of the oxide layer formed in the oxide layer forming step is held for 0.5 seconds or more in a state where it is in contact with an alkaline aqueous solution, and then washed with water and dried for neutralization.
- This neutralization treatment step will be described below.
- the alkaline aqueous solution contains 0.01 g / L or more of P ions as P concentration and 0.1 g / L or more of carbonate ions as carbonate ion concentration.
- this degreasing improvement mechanism can be considered as follows.
- the sulfuric acid acidic solution remains on the surface of the oxide layer after being washed with water and dried, the amount of etching on the surface is increased, microscopic unevenness is generated, and the affinity with oil is enhanced. Washing with an alkaline aqueous solution and complete neutralization prevents the sulfuric acid acidic solution from remaining on the surface. Further, when the alkaline aqueous solution contains P ions, the P ions adhere to the surface of the formed oxide layer. P ions are considered to contribute to degreasing properties even under severe alkaline degreasing conditions because they have a cleaning action such as being used in synthetic detergents.
- the carbonate ions are taken into the oxide layer and change the crystal structure.
- the physical properties also change, the affinity with oil decreases, and the degreasing property improves.
- the dissolution reaction of the oxide layer by P ions is reduced due to the change in physical properties, the amount of dissolution of the formed oxide layer is greatly reduced.
- the concentration of P ions contained in the alkaline aqueous solution is 0.01 g / in as P from the viewpoint of obtaining the effect by using the alkaline aqueous solution, that is, P ions adhere to the surface of the oxide layer and contribute to degreasing properties.
- P is 0.1 g / L to 20 g / L. If it is less than 0.01 g / L, P may not sufficiently adhere to the oxide layer. If it exceeds 20 g / L, the formed oxide layer may be dissolved.
- the kind of phosphorus compound which supplies P ion in alkaline aqueous solution is not specifically limited, From a cost and procurement viewpoint, it is preferable that it is 1 or more types chosen from phosphate, pyrophosphate, and a triphosphate.
- the concentration of carbonate ions in the alkaline aqueous solution is from the viewpoint of obtaining the effect of using the carbonate ions, that is, the affinity with the oil is reduced and the degreasing property is further improved, and the dissolution reaction of the oxide layer is reduced.
- the carbonate ion is set to 0.1 g / L or more. If it is less than 0.1 g / L, the incorporation of carbonate ions into the oxide layer becomes insufficient, and the physical properties cannot be changed sufficiently.
- it is 0.6 g / L to 500 g / L. In consideration of variation in concentration during production, it is more preferably 1.2 g / L or more.
- 100 g / L or less is preferable from the viewpoint of production cost.
- the carbonate ion is not particularly limited. Carbon dioxide blowing, sodium carbonate, manganese carbonate, nickel carbonate, potassium carbonate and hydrates thereof can be used. The use of carbon dioxide and carbonate exemplified above is preferable from the viewpoint of cost and procurement.
- the pH of the alkaline aqueous solution is not particularly limited as long as it is alkaline, but the pH is preferably 9-12. If pH is 9 or more, it can fully neutralize. Moreover, if pH is 12 or less, it will be easy to prevent melt
- the liquid temperature of the alkaline aqueous solution is not particularly limited, but is preferably 20 to 70 ° C. When the liquid temperature is 20 ° C. or higher, the reaction rate increases. If the liquid temperature is 70 ° C. or lower, dissolution of the oxide film is suppressed.
- the method of bringing the alkaline aqueous solution into contact with the oxide layer is not particularly limited, the method of bringing the alkaline aqueous solution into contact with the aqueous solution, the method of spraying and contacting the alkaline aqueous solution, and applying the alkaline aqueous solution onto the oxide layer using a coating roll. There are ways to do this.
- the time for contacting the alkaline aqueous solution with the oxide layer is 0.5 seconds or more. By setting it to 0.5 seconds or more, excellent degreasing properties can be imparted to the zinc-based plated steel sheet.
- the oxide layer is made of Zn, O, H, S, C, P and inevitable impurities.
- Zn is 50 mg / m 2 or more
- S is 5 mg / m 2 or more
- C is 0.2 mg / m 2 or more
- P Of 0.2 mg / m 2 or more.
- the Zn content is 50 mg / m 2 or more and that the S content is 5 mg / m 2 or more.
- the production conditions are adopted in which the galvanized steel sheet is kept in contact with the sulfuric acid acid treatment solution, held for 1 to 60 seconds, and then washed with water.
- the P content is 0.2 mg / m 2 or more. Moreover, it is preferable from a viewpoint of weldability or chemical conversion property that P content is 40 mg / m ⁇ 2 > or less.
- the C content of 0.2 mg / m 2 or more is necessary from the viewpoints of degreasing properties, appearance unevenness, and stability of press molding. Further, it is preferable from the viewpoint of weldability and chemical treatability C content is 40 mg / m 2 or less.
- the manufacturing conditions made to contact with alkaline aqueous solution containing P ion and carbonate ion are employ
- the oxide layer contains H. It is difficult to quantitatively analyze H.
- the presence of H can be confirmed by analyzing the presence form of Zn using an X-ray photoelectron spectrometer.
- Zn is present as Zn (OH) 2
- OH Zn (OH) 2
- a peak is observed around 987 eV when a narrow scan measurement of a spectrum corresponding to Zn LMM is performed using an Al Ka monochrome source.
- H There is no particular restriction on the amount of H. Since H is basically present as OH, it is considered that the amount of H increases as the amount of oxygen increases.
- a sulfate group, a carbonate group, a hydroxyl group and a phosphate group are present in the oxide layer.
- the manufacturing conditions are adopted in which the galvanized steel sheet is brought into contact with the sulfuric acid acid treatment solution and then held for 1 to 60 seconds, then washed with water and brought into contact with an alkaline aqueous solution containing carbonate ions, sulfuric acid is contained in the oxide layer.
- Groups, carbonate groups and hydroxyl groups can be present.
- the oxide layer preferably contains a crystal structure represented by Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O.
- X is a real number of 0 ⁇ X ⁇ 1
- n is a real number of 0 ⁇ n ⁇ 10.
- the oxide layer includes PO 4 3 ⁇ , P 2 O 7 4 ⁇ , P 3 O 9 5 ⁇ , and inorganic acids thereof (PO 4 3 ⁇ , P 2 O 7 4 ⁇ , P 3 O 9 5 ⁇ ). Acid) and one or more kinds selected from these metal compounds (metal compounds of PO 4 3 ⁇ , P 2 O 7 4 ⁇ , P 3 O 9 5 ⁇ ) are preferable from the viewpoint of degreasing properties.
- the metal compound is a metal containing at least one selected from PO 4 3 ⁇ , P 2 O 7 4 ⁇ and P 3 O 9 5 ⁇ and at least one selected from hydrogen, sodium and zinc.
- the content of this component is preferably such that it can be confirmed in the examples described later.
- the oxide layer is subjected to PO. 4 3 ⁇ , P 2 O 7 4 ⁇ , P 3 O 9 5 ⁇ , one or more selected from these metal compounds may be contained.
- the oxide layer may contain a metal oxide and / or hydroxide other than Zn and other components.
- S, N, P, B, Cl, Na, Mn, Ca, Mg, Ba, Sr, Si, and the like may be taken into the oxide layer due to impurities contained in the sulfuric acid acidic solution. If it is the range which does not impair the effect of, it can contain.
- an oxide layer since it is considered that an oxide is formed when the oxide layer is formed by the above mechanism, it is referred to as an “oxide layer”.
- the thickness, the Zn content, and the like are specified. As long as the above range is satisfied, the amount of oxide in the oxide layer is not particularly limited.
- the oxide layer formed in the present invention can be analyzed by the following method.
- the thickness of the oxide layer is measured using fluorescent X-ray analysis, and the obtained oxygen intensity is calculated from the value of a silicon wafer on which a silicon oxide film having a known thickness is formed. As a standard, it can be measured in terms of silica film thickness.
- a solution in which the oxide layer is dissolved with 2% ammonium dichromate + 14% ammonia water solution (% means mass%) can be quantified by analyzing using an ICP emission analyzer.
- the surface of the oxide layer is rubbed with a stainless brush and ethanol having a diameter of 0.2 mm or less and a length of 40 mm or more, and the resulting ethanol solution is filtered by suction.
- the component can be extracted as a powder component, and this can be quantified by performing a temperature rising analysis using a gas chromatograph mass spectrometer.
- crystal water it is possible to analyze the powdered oxide layer components using a differential thermogravimetric analyzer, and a weight loss of 100 ° C. or less corresponds to crystal water.
- the crystal water means water molecules taken into the crystal.
- the existence form of S, Zn and O can be analyzed using an X-ray photoelectron spectrometer.
- the existence form of P can be analyzed with an X-ray absorption fine structure apparatus.
- the crystal structure it is possible to identify the crystal structure based on the diffraction peak of the oxide layer obtained from X-ray diffraction.
- a cold-rolled steel sheet having a thickness of 0.7 mm was subjected to hot dip galvanizing treatment and alloying treatment, and then subjected to temper rolling. Subsequently, after the steel sheet was immersed in a sulfuric acid acidic solution adjusted to the conditions shown in Table 1 (Table 1-1 and Table 1-2 together to form Table 1) as an oxide layer forming treatment and squeezed with a roll The predetermined time shown in Table 1 was maintained. Next, it was washed with water and dried. Subsequently, neutralization was performed under the conditions shown in Table 1.
- a fluorescent X-ray analyzer was used to measure the thickness of the oxide layer.
- the voltage and current of the tube bulb at the time of measurement were set to 30 kV and 100 mA, the dispersive crystal was set to TAP, and OK ⁇ rays were detected.
- the intensity at the background position was also measured so that the net intensity of the O—K ⁇ ray could be calculated.
- the integration time at the peak position and the background position was 20 seconds, respectively.
- composition analysis of oxide layer Using a solution of 2% ammonium dichromate + 14% aqueous ammonia (% means% by mass), only the oxide layer is dissolved, and the solution is dissolved in an ICP emission analyzer (ICP emission analyzer). analysis of Zn, S, and P was performed.
- the surface of the oxide layer was rubbed with a stainless brush having a diameter of 0.15 mm and a length of 45 mm and ethanol, and the obtained ethanol solution was suction filtered to extract the film component as a powder component.
- the film component collected as a powder was subjected to a temperature analysis using a gas chromatograph mass spectrometer (gas-chromatograph-mass-spectrometer) to perform quantitative analysis of C.
- a pyrolysis furnace was connected to the front stage of the gas chromatograph mass spectrometer. About 2 mg of the powder sample collected in the pyrolysis furnace was inserted, and the gas generated in the pyrolysis furnace was raised from 30 ° C to 500 ° C at a heating rate of 5 ° C / min. Helium was transported into a gas chromatograph mass spectrometer and analyzed for gas composition.
- the column temperature at the time of GC / MS measurement was set to 300 ° C.
- Presence form of C The film components collected in the same manner as powder were analyzed using a gas chromatograph mass spectrometer, and the presence form of C was analyzed.
- Presence form of Zn, S, O, H The presence form of S, Zn, O was analyzed using an X-ray photoelectron spectrometer. A narrow scan measurement of a spectrum corresponding to Zn LMM, S 2p was performed using an Al Ka monochrome source.
- Presence form of P The presence form of P was analyzed using an X-ray absorption fine structure apparatus. XAFS (X-ray absorption edge fine structure *) was measured at room temperature in the beam line BL27A of High Energy Accelerator Research Organization Photon Factory.
- the degreased sample surface is irradiated with monochromated synchrotron radiation, and the absorption edge XANES (X-ray absorption edge vicinity structure **) spectrum of the P-K shell is calculated using the sample absorption current measurement. It was measured by (TEY) (total electron yield method).
- FIG. 1 is a schematic front view showing a friction coefficient measuring apparatus.
- a friction coefficient measurement sample 1 collected from a test material is fixed to a sample table 2, and the sample table 2 is fixed to the upper surface of a slide table 3 that can move horizontally.
- a slide table support 5 having a roller 4 in contact with the slide table 3 is provided on the lower surface of the slide table 3, and when this is pushed up, a pressing load N applied to the friction coefficient measurement sample 1 by the bead 6.
- a first load cell 7 is attached to the slide table support 5.
- a second load cell 8 for measuring a sliding resistance force F for moving the slide table 3 in the horizontal direction in a state where the pressing force is applied is attached to one end of the slide table 3.
- a lubricant Sugimura Chemical Industrial Co., Ltd. Wash Oil for Press Forming PRETON R352L was applied to the surface of Sample 1 and tested. .
- FIG. 2 and 3 are schematic perspective views showing the shape and dimensions of the beads used.
- the bead 6 slides with its lower surface pressed against the surface of the sample 1.
- the bead 6 shown in FIG. 2 has a width of 10 mm, a length of 5 mm in the sliding direction of the sample, and lower portions at both ends of the sliding direction are curved surfaces having a curvature of 1 mmR. It has a flat surface of 3 mm.
- the bead 6 shown in FIG. 3 has a width of 10 mm, a length of 59 mm in the sliding direction of the sample, and a lower portion at both ends in the sliding direction is formed by a curved surface having a curvature of 4.5 mmR. It has a plane with a direction length of 50 mm.
- FIG. 4 is a schematic view showing a static friction coefficient measuring apparatus using the test apparatus 10.
- the sample 100 that has been removed is pulled out.
- the constant load P and the load F necessary for pulling out the sample 100 were measured at intervals of 0.005 Hz.
- the mold 11 has a width of 35 mm, a length of 14 mm in the sliding direction of the sample, and lower portions at both ends of the sliding direction are curved surfaces having a curvature of 2 mmR.
- the lower surface of the bead to which the sample is pressed is 35 mm in width and the length in the sliding direction. It has a 10 mm plane.
- the mold 12 has a width of 35 mm, a length of 24 mm in the sliding direction of the sample, and lower portions at both ends of the sliding direction are curved surfaces having a curvature of 2 mmR, and the bottom surface of the bead against which the sample is pressed has a width of 35 mm and a sliding direction length of 20 mm. It has a plane (hereinafter, condition 3).
- a lubricating oil a cleaning oil Preton (registered trademark) R352L for press manufactured by Sugimura Chemical Co., Ltd.
- Degreasing evaluation method Degreasing was evaluated based on the water wetting rate after degreasing. After applying 2.0 g / m 2 of cleaning oil Preton R352L for press made by Sugimura Chemical Industry Co., Ltd. to the prepared test piece, FC manufactured by NIHON PARKERIZING CO., LTD. The sample was degreased using an alkaline degreasing solution of L4460. The deterioration of the alkaline degreasing liquid in the automobile production line was simulated by adding 10 g / L of pre-cleaning oil Preton R352L for press produced by Sugimura Chemical Co., Ltd. to the degreasing liquid.
- the degreasing time was 60 seconds, and the temperature was 37 ° C.
- the degreasing solution was stirred with a propeller having a diameter of 10 cm at a speed of 150 rpm.
- Degreasing was evaluated by measuring the water wetting rate of the test piece 20 seconds after the completion of degreasing.
- (4) Evaluation of appearance unevenness The appearance unevenness was evaluated visually. Based on the appearance sample shown in FIG. 5, 1-5 points were assigned for evaluation. In addition, 4 points
- No. No oxide layer formation treatment or neutralization treatment was performed.
- the comparative example 1 is inferior in press formability.
- No. No. 2 is a comparative example in which an oxide layer forming treatment and a neutralization treatment are performed, but P ions and carbonate ions are not added to the alkaline aqueous solution. Although some press moldability and appearance are good, sufficient P and C are not contained in the oxide layer, and some press moldability and degreasing properties are poor.
- No. Nos. 3 to 7 are comparative examples in which an oxide layer forming treatment and a neutralizing treatment are performed, but carbonate ions are not added to the alkaline aqueous solution.
- 50 and 51 are insufficient examples (comparative examples) in that sulfate ions are not sufficiently present in the oxide layer forming treatment liquid. Although some press moldability is good, S and C are not contained in the oxide layer, and some press moldability, degreasing, and appearance unevenness are insufficient.
- Nos. 65 to 67 are examples (comparative examples) in that P ions and carbonate ions are sufficiently present in the neutralizing solution, but the pH is outside the range of pH 9 to 12. Some press moldability is good, but sufficient C is not contained in the oxide layer, and some press moldability, degreasing properties, and appearance are insufficient.
- No. 68 is a comparative example in which no water washing is performed between the oxide formation treatment and the neutralization treatment. Some press moldability is good, but sufficient P and C are not contained in the oxide layer, and some press moldability, degreasing properties, and appearance are insufficient. No. Nos.
- composition ratio and charge balance, it should contain a crystal structure material represented by Zn 4 (SO 4 ) 0.75 (CO 3 ) 0.25 (OH) 6 ⁇ 10.0H 2 O. I understand.
- a hot-dip galvanizing treatment was performed on a cold-rolled steel sheet having a thickness of 0.7 mm, and then temper rolling was performed. Subsequently, a part of the surface activation treatment with an alkaline aqueous solution was performed using an alkaline aqueous solution adjusted to the conditions shown in Table 3. Next, as an oxide layer forming treatment, the steel sheet was immersed in a sulfuric acid acid solution adjusted to the conditions shown in Table 3, and squeezed with a roll, and then held for a predetermined time shown in Table 3. Subsequently, it was washed with water and dried. Subsequently, neutralization was performed under the conditions shown in Table 3. The sulfuric acid ion concentration in the sulfuric acid acidic solution was 15 g / L.
- the thickness of the oxide layer on the surface was measured, and press formability (sliding characteristics), degreasing properties, and appearance unevenness were evaluated by the same procedure as in Example 1. .
- No. No oxide layer formation treatment or neutralization treatment was performed.
- the comparative example of 69 is inferior in press formability.
- No. 70 is a comparative example in which the oxide layer formation treatment and the neutralization treatment are performed, but carbonate ions and P ions are not added to the alkaline aqueous solution. Sufficient P and C are not contained in the oxide layer and the press moldability and appearance are good, but the degreasing property is poor.
- No. Nos. 71 to 75 are comparative examples in which an oxide layer forming treatment and a neutralizing treatment are performed, but carbonate ions are not added to the alkaline aqueous solution.
- Sufficient C is not contained in the oxide layer, the degreasing property is insufficient, and the appearance is inferior.
- the press formability is reduced due to the dissolution of the oxide layer.
- No. Nos. 76 to 80 are invention examples in which an oxide layer forming treatment and a neutralizing treatment are performed and the conditions are also in a suitable range.
- Sufficient Zn, S, P, and C are contained in the oxide layer, and are excellent in press moldability and degreasing properties, and have a good appearance.
- No. Reference numerals 81 to 90 are invention examples in which activation treatment, oxide layer formation treatment, and neutralization treatment are performed, and the conditions are also in a suitable range.
- Example 2 confirmation of the presence of zinc hydroxide, sulfate, carbonate, pyrophosphate, crystal water in the same procedure as in Example 1, and Zn 4 (SO 4 ) 1-X ( It was investigated whether or not the crystal structure represented by CO 3 ) X (OH) 6 .nH 2 O was contained. The results of the investigation are shown in Table 4 as “O” for those whose presence and content were confirmed, and “X” for those whose presence was not confirmed (the presence or absence of crystal water is not shown in the table).
- zinc hydroxide, sulfate, carbonate, pyrophosphate, and water of crystallization are present as in Nos. 38 to 40 and 42, and Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) It can be seen that it contains a crystal structure represented by 6 ⁇ nH 2 O.
- An electrogalvanizing treatment was applied to a cold-rolled steel plate having a thickness of 0.7 mm. Subsequently, a surface activation treatment with an alkaline aqueous solution was performed using an alkaline aqueous solution adjusted to the conditions shown in Table 5. Next, as an oxide layer forming treatment, the steel sheet was immersed in a sulfuric acid acidic solution adjusted to the conditions shown in Table 5, and squeezed with a roll, and then held for a predetermined time shown in Table 5. Subsequently, it was washed with water and dried. Subsequently, neutralization was performed under the conditions shown in Table 5. The sulfuric acid ion concentration in the sulfuric acid acidic solution was 15 g / L.
- the thickness of the oxide layer on the surface of the hot dip galvanized steel sheet obtained above was measured, and the press formability (sliding characteristics) and degreasing properties were evaluated by the same procedure as in Example 1. The results obtained above are shown in Table 6.
- No. No oxide layer formation treatment or neutralization treatment was performed.
- the comparative example 91 is inferior in press formability.
- No. 92 is a comparative example in which the oxide layer forming treatment and the neutralization treatment are performed, but carbonate ions and P ions are not added to the alkaline aqueous solution. Sufficient P and C are not contained in the oxide layer and the press moldability and appearance are good, but the degreasing property is poor.
- No. Nos. 93 to 97 are comparative examples in which an oxide layer forming treatment and a neutralizing treatment are performed, but carbonate ions are not added to the alkaline aqueous solution.
- Sufficient C is not contained in the oxide layer, the degreasing property is insufficient, and the appearance is uneven.
- the press formability is reduced due to the dissolution of the oxide layer.
- No. Nos. 98 to 102 are invention examples in which an oxide layer forming treatment and a neutralizing treatment are performed, and the conditions are also in a suitable range.
- Sufficient Zn, S, P, and C are contained in the oxide layer, and are excellent in press moldability and degreasing properties, and have a good appearance.
- No. 103 to 112 are invention examples in which activation treatment, oxide layer formation treatment, and neutralization treatment are performed, and the conditions are also in a suitable range.
- Example 3 confirmation of the presence of zinc hydroxide, sulfate, carbonate, pyrophosphate, crystal water in the same procedure as in Example 1, and Zn 4 (SO 4 ) 1-X ( It was investigated whether or not the crystal structure represented by CO 3 ) X (OH) 6 .nH 2 O was contained. The results of the investigation are shown in Table 6 as ⁇ for those whose existence and content were confirmed, and x for those whose presence was not confirmed (the presence or absence of crystal water is not shown in the table).
- zinc hydroxide, sulfate, carbonate, pyrophosphate, and water of crystallization are present as in Nos. 38 to 40 and 42, and Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) It can be seen that it contains a crystal structure represented by 6 ⁇ nH 2 O.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Electrochemistry (AREA)
- Chemical Treatment Of Metals (AREA)
- Coating With Molten Metal (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
Description
上記により得られた合金化溶融亜鉛めっき鋼板に対して、表面の酸化物層の厚みを測定し、プレス成形性(摺動特性)、脱脂性および外観ムラを評価した。評価方法を以下に示す。
酸化物層の厚さ分析
酸化物層の厚みの測定には蛍光X線分析装置を使用した。測定時の管球(tube bulb)の電圧および電流は30kVおよび100mAとし、分光結晶(dispersive crystal)はTAPに設定してO-Kα線を検出した。O-Kα線の測定に際しては、そのピーク位置に加えてバックグラウンド位置での強度も測定し、O-Kα線の正味の強度が算出できるようにした。なお、ピーク位置およびバックグラウンド位置での積分時間は、それぞれ20秒とした。
重クロム酸アンモニウム2%+アンモニア水14%溶液(%は質量%を意味する)を用いて、酸化物層のみを溶解し、その溶液を、ICP発光分析装置(ICP emission spectrometry)を用いて、Zn、S、Pの定量分析を実施した。
同様に粉末化し採取した皮膜成分を、ガスクロマトブラフ質量分析計を用いて分析しCの存在形態について分析を実施した。
X線光電子分光装置を用いて、S、Zn、Oの存在形態について分析した。Al Ka モノクロ線源を使用し、Zn LMM、 S 2pに相当するスペクトルのナロースキャン測定を実施した。
Pの存在形態
X線吸収微細構造装置を用いてPの存在形態について分析した。高エネルギー加速器研究機構(High Energy Accelerator Research Organization)Photon Factoryのビームライン BL27Aにて、XAFS(X線吸収端微細構造*)の測定を室温で実施した。脱脂した試料表面に単色化した放射光を照射し、P-K殻の吸収端XANES(X線吸収端近傍構造 **)スペクトルを、試料吸収電流計測(sample absorption current measurement)による全電子収量法(TEY)(total electron yield method)で測定した。
** X-ray Absorption Near-Edge Structure 結晶水の定量
示差熱天秤(differential thermogravimetric analyzer)を用いて100℃以下の重量減少量を測定した。測定には粉末試料約15mgを用いた。試料を装置内に導入後、室温(約25℃)から1000℃まで、昇温速度10℃/minで昇温させ、昇温時の熱重量変化を記録した。
同様に粉末化し採取した皮膜成分のX線回折を実施し、結晶構造を推定した。ターゲットにはCuを用い、加速電圧40kV、管電流(tube current)50mA、スキャン速度4deg/min、スキャン範囲2~90°の条件で測定を実施した。
プレス成形性を評価するために、各供試材の摩擦係数を以下のようにして測定した。
図1は、摩擦係数測定装置を示す概略正面図である。同図に示すように、供試材から採取した摩擦係数測定用試料1が試料台2に固定され、試料台2は、水平移動可能なスライドテーブル3の上面に固定されている。スライドテーブル3の下面には、これに接したローラ4を有する上下動可能なスライドテーブル支持台5が設けられ、これを押上げることにより、ビード6による摩擦係数測定用試料1への押付荷重Nを測定するための第1ロードセル7が、スライドテーブル支持台5に取付けられている。上記押し付け力を作用させた状態でスライドテーブル3を水平方向へ移動させるための摺動抵抗力Fを測定するための第2ロードセル8が、スライドテーブル3の一方の端部に取付けられている。なお、潤滑油として、スギムラ化学工業(株)製のプレス用洗浄油プレトンR352L(Sugimura Chemical Industrial Co.,Ltd. Wash Oil for Press Forming PRETON R352L)を試料1の表面に塗布して試験を行った。
[条件1]
図2に示すビードを用い、押し付け荷重N:400kgf、試料の引き抜き速度(スライドテーブル3の水平移動速度):100cm/minとした。
[条件2]
図3に示すビードを用い、押し付け荷重N:400kgf、試料の引き抜き速度(スライドテーブル3の水平移動速度):20cm/minとした。
プレス成形シミュレーションを行った結果、面圧が7MPa以下で摺動速度が50mm/min以下の部位(張り出し成形部位など)においては、動摩擦係数より、静止摩擦係数のほうが、実際のプレス成形性との相関性が高いことが明らかになった。そこで、プレス成形性(特に張り出し部における成形性)を評価するために、各供試材の静止摩擦係数を以下のようにして測定した。図4は、試験装置10を用いた静止摩擦係数測定装置を示す概略図である。同図に示すように、供試材から採取した動摩擦係数測定用試料100を一定荷重P=370kgfで金型11、12を押し付けてから10mm/minの速度で、金型11、12で侠持されているサンプル100を引き抜く。これにより、一定荷重Pとサンプル100の引き抜きに必要な荷重Fを0.005Hzの間隔で測定した。静止摩擦係数μは、式:μ=F’/Pで算出し、摺動開始後のピーク値の摩擦係数を静止摩擦係数として取得した。なお、金型11の形状は幅35mm、試料の摺動方向長さ14mm、摺動方向両端の下部は曲率2mmRの曲面で構成され、試料が押し付けられるビード下面は幅35mm、摺動方向長さ10mmの平面を有する。金型12の形状は幅35mm、試料の摺動方向長さ24mm、摺動方向両端の下部は曲率2mmRの曲面で構成され、試料が押し付けられるビード下面は幅35mm、摺動方向長さ20mmの平面を有する(以下条件3)。なお、潤滑油として、スギムラ化学社製のプレス用洗浄油プレトン(登録商標)R352Lを試料100の表面に塗布して試験を行った。
(3)脱脂性の評価方法
脱脂性の評価は、脱脂後の水濡れ率で行った。作成した試験片に、スギムラ化学工業(株)製のプレス用洗浄油プレトンR352Lを片面2.0g/m2塗油したのち、日本パーカライジング(株)製(NIHON PARKERIZING CO.,LTD.)のFC-L4460のアルカリ脱脂液を用いてサンプルの脱脂を行った。脱脂液にスギムラ化学工業(株)製のプレス用洗浄油プレトンR352Lを10g/Lを予め添加することで自動車生産ラインにおけるアルカリ脱脂液の劣化をシミュレートした。ここで、脱脂時間は60秒とし、温度は37℃とした。脱脂時は脱脂液を直径10cmのプロペラを150rpmの速度で攪拌した。脱脂完了から20秒後の試験片の水濡れ率を測定することで、脱脂性の評価を行った。
(4)外観ムラの評価
外観ムラには目視により評価した。図5に示す外観見本を基準として、評点を1~5点を付与し評価した。なお4点以上が良好であることを示し、5点は更に良好であることを示している。
酸化物層形成処理および中和処理を行わなかったNo.1の比較例は、プレス成形性に劣る。No.2は酸化物層形成処理および中和処理を行っているが、アルカリ性水溶液中にPイオン、炭酸イオンが添加されていない比較例である。一部のプレス成形性、外観は良好であるが、酸化物層中に十分なP、Cが含まれず、一部のプレス成形性、脱脂性に劣る。
No.3~7は酸化物層形成処理および中和処理を行っているが、アルカリ性水溶液中に炭酸イオンが添加されていない比較例である。酸化物層中に十分なCが含まれず、脱脂性が不十分であり、外観ムラがある。酸化物層の溶解によりプレス成形性が低下している。
No.30はアルカリ性水溶液中にPイオンが十分に添加されていない比較例である。酸化物層中に十分なPが含まれず脱脂性が劣る。
No.37はアルカリ性水溶液中に炭酸イオンが十分に添加されていない比較例である。酸化物層中に十分なCが含まれず、酸化物層の溶解によりプレス成形性が不十分であり、脱脂性が劣っている。外観ムラがある。
No.50、51は、酸化物層の形成処理液中に硫酸イオンが十分に存在していないという点で不十分な例(比較例)である。一部のプレス成形性は良好であるが、酸化物層中にS、Cが含まれず、一部のプレス成形性、脱脂性、外観ムラも不十分である。
No.68は酸化物形成処理と中和処理の間で水洗を実施しない比較例である。一部のプレス成形性は良好であるが、酸化物層中に十分なP,Cが含まれず、一部のプレス成形性、脱脂性、外観が不十分である。
No.8~29、31~36、38~49、52~64は酸化物層形成処理および中和処理を行い、その条件も好適な範囲である発明例である。酸化物層中に十分なZn、S、P、Cが含まれ、プレス成形性および脱脂性に優れ、外観も良好である。
酸化物層形成処理および中和処理を行わなかったNo.69の比較例は、プレス成形性に劣る。
No.70は酸化物層形成処理および中和処理を行っているが、アルカリ性水溶液中に炭酸イオン及びPイオンが添加されていない比較例である。酸化物層中に十分なP、Cが含まれず、プレス成形性、外観は良好であるが、脱脂性が劣る。
No.71~75は酸化物層形成処理および中和処理を行っているが、アルカリ性水溶液中に炭酸イオンが添加されていない比較例である。酸化物層中に十分なCが含まれず、脱脂性が不十分であり、外観が劣っている。酸化物層の溶解によりプレス成形性が低下している。
No.76~80は酸化物層形成処理および中和処理を行い、その条件も好適な範囲である発明例である。酸化物層中に十分なZn、S、P、Cが含まれ、プレス成形性および脱脂性に優れ、外観も良好である。
No.81~90は活性化処理、酸化物層形成処理、中和処理を行い、その条件も好適な範囲である発明例である。酸化物層中に十分なZn、S、P、Cが含まれ、プレス成形性および脱脂性に優れ、外観も良好である。特に、No.76~79に比べプレス成形性がより一層優れているのがわかる。
酸化物層形成処理および中和処理を行わなかったNo.91の比較例は、プレス成形性に劣る。
No.92は酸化物層形成処理および中和処理を行っているが、アルカリ性水溶液中に炭酸イオン及びPイオンが添加されていない比較例である。酸化物層中に十分なP、Cが含まれず、プレス成形性、外観は良好であるが、脱脂性に劣る。
No.93~97は酸化物層形成処理および中和処理を行っているが、アルカリ性水溶液中に炭酸イオンが添加されていない比較例である。酸化物層中に十分なCが含まれず、脱脂性が不十分であり、外観ムラがある。酸化物層の溶解によりプレス成形性が低下している。
No.98~102は酸化物層形成処理および中和処理を行い、その条件も好適な範囲である発明例である。酸化物層中に十分なZn,S,P,Cが含まれ、プレス成形性および脱脂性に優れ、外観も良好である。
No.103~112は活性化処理、酸化物層形成処理、中和処理を行い、その条件も好適な範囲である発明例である。酸化物層中に十分なZn,S,P,Cが含まれ、プレス成形性および脱脂性に優れ、外観も良好である。特に、No.98~102に比べプレス成形性がより一層優れているのがわかる。
2 試料台
3 スライドテーブル
4 ローラ
5 スライドテーブル支持台
6 ビード
7 第1ロードセル
8 第2ロードセル
9 レール
N 押付荷重
F 摺動抵抗力
10 静止摩擦係数測定装置
11 金型
12 金型
100 摩擦係数測定用資料
P 押付荷重
F’ 引き抜き荷重
Claims (16)
- 鋼板と、該鋼板上に形成された亜鉛系めっき層とを備え、
前記めっき層は、表層に平均厚さ20nm以上の酸化物層を有し、
前記酸化物層は、Zn、O、H、S、C、Pおよび不可避的不純物からなり、Znを50mg/m2以上、Sを5mg/m2以上、Cを0.2mg/m2以上、Pを0.2mg/m2以上含有することを特徴とする亜鉛系めっき鋼板。 - 前記酸化物層に、硫酸基、炭酸基、水酸基及びリン酸基が存在することを特徴とする請求項1に記載の亜鉛系めっき鋼板。
- 前記酸化物層にZn4(SO4)1-X(CO3)X(OH)6・nH2Oで表される結晶構造物が含まれることを特徴とする請求項1または2に記載の亜鉛系めっき鋼板。
ここで、Xは0<X<1の実数、nは0≦n≦10の実数である。 - 前記酸化物層にPO4 3-、P2O7 4-、P3O9 5-及びこれらの無機酸又は金属化合物から選択される1種以上を含有し、
前記金属化合物は、ナトリウム及び亜鉛から選択される1種以上を含有することを特徴とする請求項1~3のいずれか1項に記載と亜鉛系めっき鋼板。 - 亜鉛系めっき鋼板は、合金化溶融亜鉛めっき鋼板、溶融亜鉛めっき鋼板又は電気亜鉛めっき鋼板であることを特徴とする請求項1~4のいずれか1項に記載の亜鉛系めっき鋼板。
- 請求項1~5のいずれか1項に記載の亜鉛系めっき鋼板の製造方法であって、
亜鉛系めっき鋼板を、硫酸イオンを含有する酸性溶液に接触させた後1~60秒間保持し、その後水洗を行う酸化物層形成工程と、
前記酸化物層形成工程で形成された酸化物層の表面を、アルカリ性水溶液に接触させた状態で0.5秒以上保持し、その後水洗、乾燥を行う中和処理工程を備え、
前記アルカリ性水溶液は、PイオンをP濃度として0.01g/L以上、炭酸イオンを炭酸イオン濃度として0.1g/L以上含有し、pHが9~12であることを特徴とする亜鉛系めっき鋼板の製造方法。 - 前記アルカリ性水溶液は、リン酸塩、ピロリン酸塩及びトリリン酸塩のうちから選ばれる1種類以上のリン化合物と、炭酸塩とを含有することを特徴とする請求項6に記載の亜鉛系めっき鋼板の製造方法。
- 前記炭酸イオンを炭酸イオン濃度として0.6g/L以上含有することを特徴とする請求項6または7に記載の亜鉛系めっき鋼板の製造方法。
- 前記炭酸イオンを炭酸イオン濃度として1.2g/L以上含有することを特徴とする請求項6~8のいずれか1項に記載の亜鉛系めっき鋼板の製造方法。
- 前記アルカリ性水溶液は、pHが9~12であり、温度が20~70℃であることを特徴とする請求項6~9のいずれか1項に記載の亜鉛系めっき鋼板の製造方法。
- 前記酸性溶液は、pH緩衝作用を有し、1Lの前記酸性溶液のpHを2.0から5.0まで上昇させるのに必要な1.0mol/L水酸化ナトリウム溶液の量(L)で定義するpH上昇度が0.003~0.5の範囲にあることを特徴とする請求項6~10のいずれか1項に記載の亜鉛系めっき鋼板の製造方法。
- 前記酸性溶液は、酢酸塩、フタル酸塩、クエン酸塩、コハク酸塩、乳酸塩、酒石酸塩、ホウ酸塩、及びリン酸塩のうちから選ばれる1種類以上の塩を合計で5~50g/L含有し、pHが0.5~5.0、液温が20~70℃であることを特徴とする請求項6~11のいずれか一項に記載の亜鉛系めっき鋼板の製造方法。
- 前記酸化物層形成工程において、前記酸性溶液接触後の鋼板表面の前記酸性溶液付着量が15g/m2以下であることを特徴とする請求項6~12のいずれか一項に記載の亜鉛系めっき鋼板の製造方法。
- 前記亜鉛系めっき鋼板は、合金化溶融亜鉛めっき鋼板、溶融亜鉛めっき鋼板、又は電気亜鉛めっき鋼板であることを特徴とする請求項6~13のいずれか1項に記載の亜鉛系めっき鋼板の製造方法。
- 鋼板に亜鉛系めっきを施した後、前記酸化物層形成工程の前に、アルカリ性の水溶液に接触させることにより表面を活性化させることを特徴とする請求項6~14のいずれか1項に記載の亜鉛系めっき鋼板の製造方法。
- 鋼板に亜鉛系めっきを施した後、前記酸化物層形成工程の前に、調質圧延を施すことを特徴とする請求項6~15のいずれか1項に記載の亜鉛系めっき鋼板の製造方法。
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP15755983.2A EP3112501B1 (en) | 2014-02-27 | 2015-02-27 | Galvanized steel sheet and method for manufacturing the same |
JP2015530230A JP5884207B2 (ja) | 2014-02-27 | 2015-02-27 | 亜鉛系めっき鋼板およびその製造方法 |
US15/121,589 US10392706B2 (en) | 2014-02-27 | 2015-02-27 | Galvanized steel sheet and method for producing the same |
MX2016011084A MX2016011084A (es) | 2014-02-27 | 2015-02-27 | Lamina de acero galvanizada y metodo para la produccion de la misma. |
CN201580010893.0A CN106062249B (zh) | 2014-02-27 | 2015-02-27 | 镀锌系钢板及其制造方法 |
KR1020167026479A KR101878220B1 (ko) | 2014-02-27 | 2015-02-27 | 아연계 도금 강판 및 그 제조 방법 |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2014036380 | 2014-02-27 | ||
JP2014-036380 | 2014-02-27 | ||
JP2014235496 | 2014-11-20 | ||
JP2014-235496 | 2014-11-20 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2015129282A1 true WO2015129282A1 (ja) | 2015-09-03 |
Family
ID=54008613
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2015/001053 WO2015129282A1 (ja) | 2014-02-27 | 2015-02-27 | 亜鉛系めっき鋼板およびその製造方法 |
Country Status (7)
Country | Link |
---|---|
US (1) | US10392706B2 (ja) |
EP (1) | EP3112501B1 (ja) |
JP (1) | JP5884207B2 (ja) |
KR (1) | KR101878220B1 (ja) |
CN (1) | CN106062249B (ja) |
MX (1) | MX2016011084A (ja) |
WO (1) | WO2015129282A1 (ja) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107109660A (zh) * | 2014-11-12 | 2017-08-29 | 杰富意钢铁株式会社 | 镀锌系钢板的制造方法 |
JP2017206716A (ja) * | 2016-05-16 | 2017-11-24 | Jfeスチール株式会社 | 鋼板およびその製造方法 |
JP2017206715A (ja) * | 2016-05-16 | 2017-11-24 | Jfeスチール株式会社 | 鋼板およびその製造方法 |
EP3428315A4 (en) * | 2016-03-11 | 2019-01-16 | JFE Steel Corporation | PROCESS FOR PRODUCING A GALVANIZED STEEL SHEET |
JP2020158879A (ja) * | 2019-03-19 | 2020-10-01 | Jfeスチール株式会社 | 溶融亜鉛系めっき鋼板の製造方法 |
JP2020164982A (ja) * | 2019-03-27 | 2020-10-08 | Jfeスチール株式会社 | 溶融亜鉛系めっき鋼板の製造方法 |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102334859B1 (ko) * | 2017-03-30 | 2021-12-02 | 제이에프이 스틸 가부시키가이샤 | 아연계 도금 강판 및 그의 제조 방법 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007016266A (ja) * | 2005-07-06 | 2007-01-25 | Jfe Steel Kk | 合金化溶融亜鉛めっき鋼板の製造方法および合金化溶融亜鉛めっき鋼板 |
JP2007119872A (ja) * | 2005-10-31 | 2007-05-17 | Jfe Steel Kk | 合金化溶融亜鉛めっき鋼板の製造方法および合金化溶融亜鉛めっき鋼板 |
JP2009127077A (ja) * | 2007-11-22 | 2009-06-11 | Jfe Steel Corp | 合金化溶融亜鉛めっき鋼板の製造方法および合金化溶融亜鉛めっき鋼板 |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2915444A (en) | 1955-12-09 | 1959-12-01 | Enthone | Process for cleaning and plating ferrous metals |
JPH03191093A (ja) | 1989-12-19 | 1991-08-21 | Nippon Steel Corp | プレス性、化成処理性に優れた亜鉛系めっき鋼板 |
JP3153098B2 (ja) | 1995-04-28 | 2001-04-03 | 新日本製鐵株式会社 | 潤滑性、化成処理性、接着剤適合性、溶接性に優れた亜鉛系めっき鋼板 |
JP3879268B2 (ja) | 1998-08-28 | 2007-02-07 | 住友金属工業株式会社 | 成形性と溶接性に優れた亜鉛系めっき鋼板の製造方法 |
JP3346338B2 (ja) * | 1999-05-18 | 2002-11-18 | 住友金属工業株式会社 | 亜鉛系めっき鋼板およびその製造方法 |
JP3608519B2 (ja) | 2001-03-05 | 2005-01-12 | Jfeスチール株式会社 | 合金化溶融亜鉛めっき鋼板の製造方法および合金化溶融亜鉛めっき鋼板 |
JP4826017B2 (ja) * | 2001-03-07 | 2011-11-30 | Jfeスチール株式会社 | 合金化溶融亜鉛めっき鋼板 |
JP3807341B2 (ja) | 2002-04-18 | 2006-08-09 | Jfeスチール株式会社 | 合金化溶融亜鉛めっき鋼板の製造方法 |
JP4135576B2 (ja) | 2002-06-28 | 2008-08-20 | Jfeスチール株式会社 | 表面処理亜鉛系めっき鋼板 |
KR20040054271A (ko) * | 2002-12-18 | 2004-06-25 | 주식회사 포스코 | 마찰특성이 우수한 합금화 용융 아연 도금강판 제조방법 |
JP4650128B2 (ja) | 2005-07-06 | 2011-03-16 | Jfeスチール株式会社 | 合金化溶融亜鉛めっき鋼板の製造方法および合金化溶融亜鉛めっき鋼板 |
JP5044976B2 (ja) | 2006-05-02 | 2012-10-10 | Jfeスチール株式会社 | 合金化溶融亜鉛めっき鋼板の製造方法および合金化溶融亜鉛めっき鋼板 |
JP5338226B2 (ja) | 2008-09-26 | 2013-11-13 | Jfeスチール株式会社 | 熱間プレス用亜鉛系めっき鋼板 |
JP5338243B2 (ja) * | 2008-10-10 | 2013-11-13 | Jfeスチール株式会社 | 熱間プレス成形用めっき鋼板およびその製造方法 |
JP5347434B2 (ja) | 2008-11-05 | 2013-11-20 | Jfeスチール株式会社 | 亜鉛系めっき鋼板の製造方法 |
JP5838542B2 (ja) | 2010-09-29 | 2016-01-06 | Jfeスチール株式会社 | 冷延鋼板の製造方法 |
MX2016017241A (es) | 2014-06-27 | 2017-04-25 | Henkel Ag & Co Kgaa | Lubricante seco para acero con recubrimiento de zinc. |
JP6822127B2 (ja) * | 2016-06-23 | 2021-01-27 | Tdk株式会社 | 磁気センサ |
-
2015
- 2015-02-27 MX MX2016011084A patent/MX2016011084A/es unknown
- 2015-02-27 US US15/121,589 patent/US10392706B2/en active Active
- 2015-02-27 KR KR1020167026479A patent/KR101878220B1/ko active IP Right Grant
- 2015-02-27 CN CN201580010893.0A patent/CN106062249B/zh active Active
- 2015-02-27 JP JP2015530230A patent/JP5884207B2/ja active Active
- 2015-02-27 EP EP15755983.2A patent/EP3112501B1/en active Active
- 2015-02-27 WO PCT/JP2015/001053 patent/WO2015129282A1/ja active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007016266A (ja) * | 2005-07-06 | 2007-01-25 | Jfe Steel Kk | 合金化溶融亜鉛めっき鋼板の製造方法および合金化溶融亜鉛めっき鋼板 |
JP2007119872A (ja) * | 2005-10-31 | 2007-05-17 | Jfe Steel Kk | 合金化溶融亜鉛めっき鋼板の製造方法および合金化溶融亜鉛めっき鋼板 |
JP2009127077A (ja) * | 2007-11-22 | 2009-06-11 | Jfe Steel Corp | 合金化溶融亜鉛めっき鋼板の製造方法および合金化溶融亜鉛めっき鋼板 |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107109660A (zh) * | 2014-11-12 | 2017-08-29 | 杰富意钢铁株式会社 | 镀锌系钢板的制造方法 |
EP3428315A4 (en) * | 2016-03-11 | 2019-01-16 | JFE Steel Corporation | PROCESS FOR PRODUCING A GALVANIZED STEEL SHEET |
US10443116B2 (en) | 2016-03-11 | 2019-10-15 | Jfe Steel Corporation | Method for manufacturing zinc-based coated steel sheet |
JP2017206716A (ja) * | 2016-05-16 | 2017-11-24 | Jfeスチール株式会社 | 鋼板およびその製造方法 |
JP2017206715A (ja) * | 2016-05-16 | 2017-11-24 | Jfeスチール株式会社 | 鋼板およびその製造方法 |
JP2020158879A (ja) * | 2019-03-19 | 2020-10-01 | Jfeスチール株式会社 | 溶融亜鉛系めっき鋼板の製造方法 |
JP6992831B2 (ja) | 2019-03-19 | 2022-02-15 | Jfeスチール株式会社 | 溶融亜鉛系めっき鋼板の製造方法 |
JP2020164982A (ja) * | 2019-03-27 | 2020-10-08 | Jfeスチール株式会社 | 溶融亜鉛系めっき鋼板の製造方法 |
JP7036137B2 (ja) | 2019-03-27 | 2022-03-15 | Jfeスチール株式会社 | 溶融亜鉛系めっき鋼板の製造方法 |
Also Published As
Publication number | Publication date |
---|---|
US20160369406A1 (en) | 2016-12-22 |
CN106062249B (zh) | 2019-07-02 |
JPWO2015129282A1 (ja) | 2017-03-30 |
EP3112501A1 (en) | 2017-01-04 |
US10392706B2 (en) | 2019-08-27 |
CN106062249A (zh) | 2016-10-26 |
JP5884207B2 (ja) | 2016-03-15 |
EP3112501B1 (en) | 2020-11-04 |
KR20160122265A (ko) | 2016-10-21 |
KR101878220B1 (ko) | 2018-07-13 |
EP3112501A4 (en) | 2017-11-22 |
MX2016011084A (es) | 2016-11-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5884207B2 (ja) | 亜鉛系めっき鋼板およびその製造方法 | |
JP5884206B2 (ja) | 亜鉛系めっき鋼板およびその製造方法 | |
KR101788950B1 (ko) | 아연계 도금 강판의 제조 방법 | |
WO2017154495A1 (ja) | 亜鉛系めっき鋼板の製造方法 | |
JP4517887B2 (ja) | 溶融亜鉛めっき鋼板の製造方法および溶融亜鉛めっき鋼板 | |
JP6610421B2 (ja) | 鋼板およびその製造方法 | |
JP5648308B2 (ja) | 摺動性に優れる亜鉛系めっき鋼板 | |
JP5648309B2 (ja) | 溶融亜鉛系めっき鋼板の製造方法 | |
JP2005248262A (ja) | 電気亜鉛めっき鋼板、その製造方法及び製造装置 | |
JP2010077455A (ja) | 合金化溶融亜鉛めっき鋼板およびその製造方法 | |
JP2010090401A (ja) | Zn−Al系めっき鋼板およびその製造方法 | |
JP5163218B2 (ja) | 亜鉛系めっき鋼板の製造方法 | |
JP6992831B2 (ja) | 溶融亜鉛系めっき鋼板の製造方法 | |
JP6610420B2 (ja) | 鋼板およびその製造方法 | |
JP5961967B2 (ja) | 溶融亜鉛めっき鋼板の製造方法 | |
JP5927995B2 (ja) | 亜鉛系めっき鋼板の製造方法 | |
JP2009235432A (ja) | 亜鉛系めっき鋼板およびその製造方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
ENP | Entry into the national phase |
Ref document number: 2015530230 Country of ref document: JP Kind code of ref document: A |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 15755983 Country of ref document: EP Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 15121589 Country of ref document: US Ref document number: MX/A/2016/011084 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: 20167026479 Country of ref document: KR Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: IDP00201606455 Country of ref document: ID |
|
REEP | Request for entry into the european phase |
Ref document number: 2015755983 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2015755983 Country of ref document: EP |