WO2016075920A1 - Method for manufacturing galvanized steel sheet - Google Patents
Method for manufacturing galvanized steel sheet Download PDFInfo
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- WO2016075920A1 WO2016075920A1 PCT/JP2015/005583 JP2015005583W WO2016075920A1 WO 2016075920 A1 WO2016075920 A1 WO 2016075920A1 JP 2015005583 W JP2015005583 W JP 2015005583W WO 2016075920 A1 WO2016075920 A1 WO 2016075920A1
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- steel sheet
- aqueous solution
- alkaline aqueous
- zinc
- galvanized steel
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- 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
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- 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
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- 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
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- 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
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- 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
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- 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
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/14—Cleaning or pickling metallic material with solutions or molten salts with alkaline solutions
- C23G1/20—Other heavy metals
Definitions
- the present invention relates to a method for producing a galvanized steel sheet having a reaction layer.
- Zinc-based plated steel sheets are used in a wide range of applications, mainly in automobile bodies, home appliances, and building materials. With respect to galvanized steel sheets for such applications, a technique is known in which a reaction layer is provided on the surface of the steel sheet to improve properties such as press molding, corrosion resistance, and appearance.
- the galvanized steel sheet before forming the reaction layer conventionally has an unnecessary oxide layer such as Zn having a thickness of less than 10 nm and Al being an impurity element in the outermost layer.
- This unnecessary oxide layer hinders the reactivity of chemical conversion treatment such as zinc phosphate treatment and chromate treatment, and it is necessary to set a long reaction time in order to form a sufficient reaction layer.
- the increase in reaction time is accompanied by an increase in equipment costs and line length, and an increase in running costs such as electricity and gas.
- Patent Document 1 describes a technique in which a hot-dip galvanized steel sheet is contacted with an alkaline aqueous solution and then treated with a SiO 2 -containing chromate solution.
- Patent Documents 2 and 3 describe techniques for forming an oxide layer after contacting a hot-dip galvanized steel sheet with an alkaline aqueous solution.
- Patent Document 4 describes a technique for forming an oxide layer after bringing the surface of an alloyed hot-dip galvanized steel sheet into contact with an alkaline aqueous solution.
- Patent Document 5 discloses a crystal structure represented by Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O after contacting the surface of a hot dip galvanized steel sheet with an alkaline aqueous solution. A technique for forming an oxide layer containing an object is described.
- the present invention has been made in view of such circumstances.
- Zinc-based plated steel sheet that can remove unnecessary oxide layers on the surface of the zinc-based plating layer by contact with an alkaline aqueous solution, and can avoid appearance problems due to precipitates that precipitate in the alkaline aqueous solution. It aims at providing the manufacturing method of.
- the present inventors have intensively studied to solve the above problems. As a result, the inventors have found that the above problem can be solved by adding a specific chelating agent to the alkaline aqueous solution used before forming the reaction layer, and have completed the present invention. More specifically, the present invention provides the following.
- the method for producing a zinc-based plated steel sheet according to the first invention for solving the above-mentioned problem is a method for producing a zinc-based plated steel sheet having a reaction layer on the surface of the steel sheet, and the reaction layer is Zn 4 (SO 4 ).
- X (CO 3 ) X (OH) 6 ⁇ nH 2 O is an oxide layer containing a crystal structure, and as a pretreatment for forming the reaction layer, sodium gluconate, sodium glucoheptonate, Contains at least 0.050 mass% of a total of one or more chelating agents selected from sodium acid, tartaric acid, arabonic acid, galactonic acid, sorbit, mannitol, glycerin, EDTA, sodium tripolyphosphate, and has a pH of 10.0 or more
- the zinc-based plated steel sheet is brought into contact with an alkaline aqueous solution for 1.0 second or longer.
- the method for producing a zinc-based plated steel sheet according to the second invention for solving the above problem is the method for producing a zinc-based plated steel sheet according to the first invention, wherein the pH of the alkaline aqueous solution is 12.6 or more. It is characterized by that.
- the oxide on the surface of the zinc-based plating layer can be satisfactorily removed by contact with an alkaline aqueous solution.
- precipitates of Al and Zn and the like can be reduced, and a galvanized steel sheet having a reaction layer with a good appearance can be obtained.
- FIG. 1 is a schematic diagram showing evaluation criteria for evaluating appearance unevenness.
- the zinc-based plated steel sheet is a steel sheet having a coating mainly composed of zinc on the surface of the steel sheet regardless of the production method, such as a zinc-plated steel sheet, a zinc alloy-plated steel sheet, and a plated steel sheet in which particles are dispersed in zinc.
- the zinc-based plating layer includes a zinc plating layer, a zinc alloy plating layer, a plating layer in which particles are dispersed in zinc, and the like.
- the present invention provides a reaction layer that can satisfactorily remove an unnecessary oxide layer present on the surface of a zinc-based plating layer, that is, Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2
- the present invention includes, for example, a step of applying zinc plating, a step of contacting with an alkaline aqueous solution, and a crystal structure represented by Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O Forming an oxide layer containing an object.
- each step will be described.
- the process of applying zinc-based plating will be described.
- the method of 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
- elemental components other than Al are not particularly limited. That is, even if Pb, Sb, Si, Sn, Mg, Mn, Ni, Ti, Li, Cu or the like is contained in addition to Al, the effect of the present invention is not impaired.
- the steel type of the steel sheet to be galvanized is not particularly limited, and various steel sheets such as a low carbon steel, an ultra low carbon steel, an IF steel, and a high strength steel sheet added with various alloy elements should be used. Can do. Moreover, both a hot-rolled steel plate and a cold-rolled steel plate can be used as the steel plate.
- the thickness of the steel plate is not particularly limited. From the viewpoint of use in applications such as automobile bodies, home appliances, and building materials, 0.4 to 5.0 mm is preferable.
- an alloyed hot-dip galvanized steel sheet that has been subjected to alloying treatment after hot-dip galvanizing may be used.
- the conditions for the alloying treatment are not particularly limited, and preferable conditions may be adopted as appropriate.
- a contact treatment using an alkaline aqueous solution is performed.
- the alkaline aqueous solution used in this contact treatment has a pH of 10.0 or higher. If the pH is less than 10.0, the removal of the oxide layer becomes insufficient. When the pH is 12.6 or more, the contact time with the alkaline aqueous solution can be shortened, which is effective and preferable. On the other hand, pH of 14.0 or less is preferable from the viewpoint of preventing dissolution of the zinc-based plating layer and preventing blackening of the surface appearance.
- the alkaline aqueous solution contains a total of 0.050 mass% or more of a specific chelating agent.
- a specific chelating agent When the deposits of Al and Zn increase in the alkaline aqueous solution, the appearance of the liquid becomes a suspension.
- 0.055 mass% or more of a chelating agent is contained in an alkaline aqueous solution, and precipitates of Al and Zn are reduced.
- the chelating agent is at least one selected from sodium gluconate, sodium glucoheptonate, sodium citrate, tartaric acid, arabonic acid, galactonic acid, sorbit, mannitol, glycerin, EDTA, and sodium tripolyphosphate. From the viewpoint of being able to chelate Al and Zn and being inexpensive, the chelating agent is preferably sodium gluconate.
- the amount of the chelating agent contained in the alkaline aqueous solution is preferably 0.100 mass% or more.
- the amount of chelating agent contained in the alkaline aqueous solution is preferably 10.0 mass% or less.
- the temperature of the alkaline aqueous solution is preferably in the range of 20 ° C. to 70 ° C., more preferably 40 ° C. to 70 ° C.
- the type of alkali builder is not limited. It is preferable to use chemicals such as NaOH from the viewpoint of cost reduction. In order to achieve the desired pH of the alkaline aqueous solution, the amount of alkali builder is appropriately adjusted. Further, the alkaline aqueous solution may contain substances other than the elements contained in the zinc-based plating solution such as Zn, Al, Fe, and other components.
- the time for contacting the galvanized steel sheet with the alkaline aqueous solution is 1.0 second or more.
- the contact time is less than 1.0 second, the oxide on the surface of the zinc-based plating layer cannot be sufficiently removed, and thus the reaction time for providing the reaction layer is not sufficiently shortened.
- the time for contacting the zinc-based plated steel sheet with the alkaline aqueous solution is preferably 10.0 seconds or less.
- temper rolling may be performed either after the step of applying zinc-based plating and before or after the alkaline aqueous solution treatment. Since the site
- reaction layer Usually, the steel sheet is brought into contact with an alkaline aqueous solution and then washed and dried, and then the reaction layer, that is, Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O A treatment for providing an oxide layer containing a crystalline structure is performed.
- the oxide layer containing a crystal structure represented by Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O is a zinc-based plating and chemical treatment solution. Is a layer of a reaction product formed on the surface of the steel sheet due to contact and chemical reaction.
- a treatment for forming an oxide layer containing a crystal structure represented by Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O for example, a zinc-based plated steel sheet is treated with sulfuric acid. Contact with an acidic solution containing ions, hold for 1 to 60 seconds, and then wash with water.
- the neutralization process process which carries out washing
- the alkaline aqueous solution may contain 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.
- the present invention is not limited to this treatment method as long as the crystal structure represented by Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O exists on the surface of the steel sheet. is not.
- Temper rolling was performed on a steel sheet obtained by subjecting a cold-rolled steel sheet having a thickness of 0.7 mm and a width of 1100 mm to a hot dip galvanizing treatment. Subsequently, as a treatment for removing the oxide layer, the steel sheet was contacted with an alkaline aqueous solution adjusted to the conditions shown in Tables 1-1 and 1-2 for a specified time, washed with water, and dried.
- the cold-rolled steel sheet subjected to electrogalvanization treatment was brought into contact with an alkaline aqueous solution in the same procedure, then washed with water and dried.
- the thickness of the unnecessary oxide layer on the surface of the zinc-based plating layer after the alkaline aqueous solution treatment and the appearance unevenness after the formation of the reaction layer are evaluated and included in the alkaline aqueous solution.
- Suspension material (SS) was measured.
- pH of alkaline aqueous solution was measured with the commercially available glass electrode.
- an oxide layer forming treatment including a crystal structure represented by Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O
- 30 g of sodium acetate trihydrate was added.
- the steel sheet was immersed in a sulfuric acid solution containing / L and adjusted to pH 1.5, squeezed with a roll, and held for 10 seconds. Next, it was washed with water and dried. Subsequently, neutralization was performed with a treatment solution containing sodium pyrophosphate 9.8 g / L and sodium carbonate decahydrate 0.48 g / L.
- a fluorescent X-ray analyzer was used to measure the thickness of the unnecessary oxide layer formed on the galvanized steel sheet. If the thickness (oxide film thickness) of the oxide layer is 4 nm or less, it can be evaluated that the reaction time for providing the reaction layer is shortened. If it is 2 nm or less, it can be evaluated that the reaction time is further shortened.
- the voltage and current of the tube at the time of measurement were 30 kV and 100 mA, the spectroscopic crystal was set to TAP, and the O-K ⁇ ray was 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.
- the various plated steel sheets were applied to a thickness of 3 ⁇ m, held for 10 seconds, then washed with water and dried to form an oxide layer.
- the observation area is 70 mm ⁇ 150 mm.
- 1 to 5 points were assigned for evaluation. Four points indicate that it is good, and five points indicate that it is even better.
- Table 1-1 and 1-2 show the following matters.
- No. 1 to 57 were subjected to surface analysis after removing an unnecessary oxide layer with an alkaline aqueous solution.
- No. 4 and 11 are examples (comparative examples) in which the concentration of the chelating agent is insufficient, although the contact with the alkaline aqueous solution containing the chelating agent is performed.
- the oxide layer can be sufficiently removed.
- suspended substances are generated in the alkaline aqueous solution.
- No. 19 and 23 are examples (comparative examples) in which the contact time is short although the contact with the alkaline aqueous solution containing the chelating agent is carried out.
- the oxide layer has a thickness of 6 to 7 nm and cannot be removed sufficiently.
- No. Nos. 27 and 34 are examples (comparative examples) in which the pH is low although contact with an alkaline aqueous solution containing a chelating agent is carried out.
- the thickness of the oxide layer is 7 nm and cannot be removed sufficiently.
- No. 24 and 28 to 33 are examples of the present invention in which the influence of pH was confirmed at a contact time of 1.0 second.
- the pH is 12.6 or more, the oxide film can be removed to 2 nm or less even when the contact time is 1.0 second, and the reaction time for providing the reaction layer can be further shortened.
- Presence form of C Similarly, the coating component collected by pulverization was analyzed using gas chromatography bluff mass spectrometry, 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. Using an Al Ka monochromatic radiation source, narrow measurement of the spectrum corresponding to Zn LMM, S 2p was performed.
- Presence form of P was analyzed using an X-ray absorption fine structure apparatus. Measurement of ZAFS (X-ray absorption fine structure) was carried out at room temperature in the beam line BL27A of Photon Factory of the High Energy Accelerator Research Organization. The degreased sample surface was irradiated with monochromated synchrotron radiation, and the absorption edge XANES (structure near the X-ray absorption edge) spectrum of the PK shell was measured by the total electron yield method (TEY) based on the sample absorption current measurement.
- TEY total electron yield method
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Abstract
Description
先ず、亜鉛系めっきを施す工程について説明する。亜鉛系めっきを施す工程において、亜鉛めっきを施す方法は特に限定されず、溶融亜鉛めっき、電気亜鉛めっき等の一般的な方法を採用可能である。また、電気亜鉛めっき、溶融亜鉛めっきの処理条件は、特に限定されず、適宜好ましい条件を採用すればよい。なお、溶融亜鉛めっきを行う場合、めっき浴中にAlが添加されていることがドロス対策の観点から好ましい。この場合Al以外の元素成分は特に限定されない。すなわち、Alの他に、Pb、Sb、Si、Sn、Mg、Mn、Ni、Ti、Li、Cuなどが含有されていても、本発明の効果が損なわれるものではない。 -Zinc-based plating process-
First, the process of applying zinc-based plating will be described. In the step of applying zinc-based plating, the method of applying zinc plating is not particularly limited, and general methods such as hot dip galvanizing and electrogalvanizing can be employed. Moreover, the process conditions of electrogalvanization and hot dip galvanization are not specifically limited, What is necessary is just to employ | adopt preferable conditions suitably. In addition, when performing hot dip galvanization, it is preferable from the viewpoint of dross countermeasure that Al is added in the plating bath. In this case, elemental components other than Al are not particularly limited. That is, even if Pb, Sb, Si, Sn, Mg, Mn, Ni, Ti, Li, Cu or the like is contained in addition to Al, the effect of the present invention is not impaired.
亜鉛系めっき処理を施した後、アルカリ性水溶液を用いた接触処理を行う。この接触処理で用いるアルカリ性水溶液はpH10.0以上である。pH10.0未満では、酸化物層の除去が不十分となる。pHが12.6以上だとアルカリ水溶液との接触時間を短縮することができ効果的であり、好ましい。
一方、亜鉛系めっき層の溶解防止、表面外観の黒化防止の観点から、pH14.0以下が好ましい。 -Step of contact with alkaline aqueous solution-
After the zinc plating treatment is performed, a contact treatment using an alkaline aqueous solution is performed. The alkaline aqueous solution used in this contact treatment has a pH of 10.0 or higher. If the pH is less than 10.0, the removal of the oxide layer becomes insufficient. When the pH is 12.6 or more, the contact time with the alkaline aqueous solution can be shortened, which is effective and preferable.
On the other hand, pH of 14.0 or less is preferable from the viewpoint of preventing dissolution of the zinc-based plating layer and preventing blackening of the surface appearance.
通常は、鋼板をアルカリ性水溶液と接触させた後に水洗・乾燥を行い、その後に反応層、すなわち、Zn4(SO4)1-X(CO3)X(OH)6・nH2Oで表される結晶構造物が含まれる酸化物層を設けるための処理を実施する。 -Process of forming reaction layer-
Usually, the steel sheet is brought into contact with an alkaline aqueous solution and then washed and dried, and then the reaction layer, that is, Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O A treatment for providing an oxide layer containing a crystalline structure is performed.
アルカリ性水溶液との接触後、亜鉛系めっき鋼板に形成された不要な酸化物層の厚さの測定には蛍光X線分析装置を使用した。酸化物層の厚さ(酸化膜厚)が4nm以下であれば、反応層を設けるための反応時間を短縮化したと評価できる。2nm以下であれば更に反応時間を短縮したと評価できる。 (1) Measurement of unnecessary oxide layer thickness After contact with the alkaline aqueous solution, a fluorescent X-ray analyzer was used to measure the thickness of the unnecessary oxide layer formed on the galvanized steel sheet. If the thickness (oxide film thickness) of the oxide layer is 4 nm or less, it can be evaluated that the reaction time for providing the reaction layer is shortened. If it is 2 nm or less, it can be evaluated that the reaction time is further shortened.
アルカリ性水溶液で接触処理した溶融亜鉛めっき鋼板、合金化溶融亜鉛めっき鋼板、電気亜鉛めっき鋼板に対して、表面に酸化物層を形成する処理を実施した後、外観ムラを目視及び顕微鏡観察により評価した。即ち、硫酸第1鉄を5.0g/L、酢酸ナトリウム・7水和物を50g/L含有する水溶液を硫酸でpH2.0に調整した液を準備し、この処理液をアルカリ性水溶液で接触処理した各種めっき鋼板に3μmの厚さになるように塗布し、10秒間保持した後、水洗・乾燥を行い、酸化物層を形成する処理を実施した。なお、観察面積は70mm×150mmである。図1に示す外観見本を基準として、評点を1~5点で付与し評価した。4点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。 (2) Evaluation of appearance unevenness and oxide film thickness after surface oxidation treatment Treatment for forming an oxide layer on the surface of hot-dip galvanized steel sheet, alloyed hot-dip galvanized steel sheet, and electrogalvanized steel sheet contact-treated with an alkaline aqueous solution Then, the appearance unevenness was evaluated by visual observation and microscopic observation. That is, a solution in which an aqueous solution containing ferrous sulfate 5.0 g / L and sodium acetate heptahydrate 50 g / L was adjusted to pH 2.0 with sulfuric acid was prepared, and this treatment solution was contact-treated with an alkaline aqueous solution. The various plated steel sheets were applied to a thickness of 3 μm, held for 10 seconds, then washed with water and dried to form an oxide layer. The observation area is 70 mm × 150 mm. Based on the appearance sample shown in FIG. 1, 1 to 5 points were assigned for evaluation. Four points indicate that it is good, and five points indicate that it is even better.
亜鉛系めっき鋼板100t処理以降のアルカリ性水溶液を採取し、孔径1μmのメンブレンフィルターを用いて吸引ろ過した。ろ過物質を110℃で乾燥した後重量を測定し、mg/Lに換算した。この値が10mg/Lを超えた製造量を記録した。10mg/Lを超える鋼板処理量が3000t以上であれば、生産性の点から良好と評価できる。また、5000t処理後も、10mg/Lを超えなかったものについては、懸濁物質なし(表1-1、1-2中では「>5000」と表記)と評価した。アルカリ水溶液処理を行っていないNo.1、54及び56はこの測定を実施しなかった。 (3) Measurement of suspended solids (SS) An alkaline aqueous solution after the treatment of the zinc-based plated steel sheet 100t was collected and suction filtered using a membrane filter having a pore diameter of 1 μm. The filtered material was dried at 110 ° C., and the weight was measured and converted to mg / L. The production amount at which this value exceeded 10 mg / L was recorded. If the amount of steel sheet processing exceeding 10 mg / L is 3000 t or more, it can be evaluated as favorable from the viewpoint of productivity. Those that did not exceed 10 mg / L even after 5000 t treatment were evaluated as having no suspended solids (denoted as “> 5000” in Tables 1-1 and 1-2). No. No treatment with alkaline aqueous solution. 1, 54 and 56 did not make this measurement.
Zn4(SO4)1-X(CO3)X(OH)6・nH2Oで表される結晶構造物が含まれる酸化物層を、直径0.15mm、長さ45mmのステンレスブラシとエタノールを用いて表面をこすり、得られたエタノール液を吸引ろ過することで、皮膜成分を粉末成分として抽出した。粉末として採取した皮膜成分を、ガスクロマトグラフ質量分析計を用いて昇温分析することでCの定量分析を実施した。ガスクロマトグラフ質量分析計の前段に熱分解炉を接続した。熱分解炉内に採取した粉末試料を約2mg挿入し、熱分解炉の温度を30℃から500℃まで、昇温速度5℃/minで昇温させた、熱分解炉内で発生するガスをヘリウムでガスクロマトグラフ質量分析計内に搬送し、ガス組成を分析した。GC/MS測定時のカラム温度は300℃に設定した。 (4) Zn 4 (SO 4 ) in 1-X (CO 3) X (OH) 6 · nH 2 O Checking Zn 4 (SO 4) 1- X (CO 3) X (OH) 6 · nH 2 O The surface of the oxide layer containing the crystal structure represented is rubbed with a stainless steel brush with a diameter of 0.15 mm and a length of 45 mm and ethanol, and the resulting ethanol solution is suction filtered to powder the film components. Extracted as a component. The film component collected as a powder was subjected to temperature analysis using a 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.
同様に粉末化し採取した皮膜成分、ガスクロマトブラフ質量分析を用いて分析しCの存在形態について分析を実施した。 Presence form of C Similarly, the coating component collected by pulverization was analyzed using gas chromatography bluff mass spectrometry, and the presence form of C was analyzed.
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測定を実施した。 Presence form of Zn, S, O, H The presence form of S, Zn, O was analyzed using an X-ray photoelectron spectrometer. Using an Al Ka monochromatic radiation source, narrow measurement of the spectrum corresponding to Zn LMM, S 2p was performed.
X線吸収微細構造装置を用いてPの存在状態について分析した。高エネルギー加速器研究機構Photon Factoryのビームライン BL27Aにて、ZAFS(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、試料吸収電流計測による全電子収量法(TEY)で測定した。 Presence form of P The presence state of P was analyzed using an X-ray absorption fine structure apparatus. Measurement of ZAFS (X-ray absorption fine structure) was carried out at room temperature in the beam line BL27A of Photon Factory of the High Energy Accelerator Research Organization. The degreased sample surface was irradiated with monochromated synchrotron radiation, and the absorption edge XANES (structure near the X-ray absorption edge) spectrum of the PK shell was measured by the total electron yield method (TEY) based on the sample absorption current measurement.
結晶水の定量
示差熱天秤を用いて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。[Correction based on Rule 91 26.11.2015]
Determination of water of crystallization The weight loss of 100 ° C. or less was measured using a differential thermobalance. About 15 mg of powder sample was used for the measurement. After the sample was introduced into the apparatus, the temperature was raised from room temperature (about 25 ° C.) to 1000 ° C. at a rate of temperature rise of 10 ° C./min, and the thermogravimetric change at the time of temperature rise was recorded.
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。 Identification of Crystal Structure X-ray diffraction was performed on the film components collected by pulverization in the same manner, and the crystal structure was estimated. Cu was used as a target, and measurement was performed under the conditions of an acceleration voltage of 40 kV, a tube current of 50 mA, a scan speed of 4 deg / min, and a scan range of 2 to 90 °.
示差熱天秤の結果から、100℃以下に11.2%の重量減少が認められ、結晶水を含有していることが分かった。[Correction based on Rule 91 26.11.2015]
From the results of the differential thermal balance, it was found that a weight loss of 11.2% was observed at 100 ° C. or lower, and it contained crystal water.
示差熱天秤の結果から、100℃以下に9.4%の重量減少が認められ、結晶水を含有していることが分かった。[Correction based on Rule 91 26.11.2015]
From the results of the differential thermobalance, it was found that a weight loss of 9.4% was observed at 100 ° C. or lower, and it contained crystal water.
Claims (2)
- 鋼板の表面に反応層を有する亜鉛系めっき鋼板の製造方法であって、前記反応層はZn4(SO4)1-X(CO3)X(OH)6・nH2Oで表される結晶構造物が含まれる酸化物層であり、前記反応層形成の前処理として、グルコン酸ナトリウム、グルコヘプトン酸ナトリウム、クエン酸ナトリウム、酒石酸、アラボン酸、ガラクトン酸、ソルビット、マンニット、グリセリン、EDTA、トリポリリン酸ナトリウムの中から選ばれる1種以上のキレート剤を合計0.050mass%以上含有しpHが10.0以上のアルカリ性水溶液に亜鉛系めっき鋼板を1.0秒以上接触させることを特徴とする亜鉛系めっき鋼板の製造方法。 A method for producing a zinc-based plated steel sheet having a reaction layer on the surface of the steel sheet, wherein the reaction layer is a crystal represented by Zn 4 (SO 4 ) 1-X (CO 3 ) X (OH) 6 .nH 2 O An oxide layer containing a structure, and as a pretreatment for forming the reaction layer, sodium gluconate, sodium glucoheptate, sodium citrate, tartaric acid, arabonic acid, galactonic acid, sorbit, mannitol, glycerin, EDTA, tripolylin Zinc, characterized by bringing a zinc-based plated steel sheet into contact with an alkaline aqueous solution containing 0.050 mass% or more of a total of one or more chelating agents selected from sodium acid and having a pH of 10.0 or more for 1.0 second or more Manufacturing method of a galvanized steel sheet.
- 前記アルカリ性水溶液のpHが12.6以上であ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の製造方法。 The method for producing a galvanized steel sheet according to claim 1, wherein the pH of the alkaline aqueous solution is 12.6 or more.
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KR1020177012379A KR102007103B1 (en) | 2014-11-12 | 2015-11-09 | Method for manufacturing steel sheet coated with zinc-based coating layer |
US15/526,140 US20170314138A1 (en) | 2014-11-12 | 2015-11-09 | Method for manufacturing steel sheet coated with zinc-based coating layer (as amended) |
JP2016512140A JPWO2016075920A1 (en) | 2014-11-12 | 2015-11-09 | Method for producing galvanized steel sheet |
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US2915444A (en) * | 1955-12-09 | 1959-12-01 | Enthone | Process for cleaning and plating ferrous metals |
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JP4604712B2 (en) | 2004-12-27 | 2011-01-05 | Jfeスチール株式会社 | Method for producing hot dip galvanized steel sheet and hot dip galvanized steel sheet |
JP4517887B2 (en) | 2005-02-25 | 2010-08-04 | Jfeスチール株式会社 | Method for producing hot dip galvanized steel sheet and hot dip galvanized steel sheet |
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TWI394863B (en) * | 2007-12-27 | 2013-05-01 | Kansai Paint Co Ltd | Metal surface treatment composition, and surface-treated metal material with metal surface treatment layer obtained from the metal surface treatment composition |
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JPS63213682A (en) * | 1987-03-02 | 1988-09-06 | Nisshin Steel Co Ltd | Surface treatment of galvanized steel sheet |
JP2007169772A (en) * | 2005-12-20 | 2007-07-05 | Nippon Denro Kk | Coloring treatment method for hot dip galvanizing surface |
WO2015129283A1 (en) * | 2014-02-27 | 2015-09-03 | Jfeスチール株式会社 | Galvanized steel sheet and method for manufacturing same |
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