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(11) | EP 3 115 482 A1 |
| (12) | EUROPEAN PATENT APPLICATION |
| published in accordance with Art. 153(4) EPC |
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| (54) | COLD-ROLLED STEEL SHEET, MANUFACTURING METHOD THEREFOR, AND CAR PART |
| (57) There are provided a cold-rolled steel sheet having excellent chemical convertibility
and high corrosion resistance after coating and a method for producing the cold-rolled
steel sheet, and an automotive component. The method includes performing first pickling with an acid liquid 1) or an acid liquid 2) below on a steel sheet subjected to continuous annealing after cold-rolling and performing second pickling with an acid liquid made of a non-oxidizing acid on the steel sheet: the acid liquid 1) containing nitric acid and hydrochloric acid, in which the nitric acid has a concentration of more than 50 g/L to 200 g/L or less, a ratio R1 (hydrochloric acid/nitric acid) of a concentration of the hydrochloric acid to the concentration of the nitric acid is 0.01 to 0.25, and a concentration of iron ions is 3 to 50 g/L, and the acid liquid 2) containing nitric acid and hydrofluoric acid, in which the nitric acid has a concentration of more than 50 g/L to 200 g/L or less, a ratio R2 (hydrofluoric acid/nitric acid) of a concentration of the hydrofluoric acid to the concentration of the nitric acid is 0.01 to 0.25, and a concentration of iron ions is 3 to 50 g/L. |
[Technical Field]
[0001] The present invention relates to a cold-rolled steel sheet and a method for producing the steel sheet, and an automotive component. In particular, the present invention relates to a cold-rolled steel sheet having excellent chemical convertibility and high corrosion resistance after coating, which is evaluated by a hot salt water immersion test or a combined cyclic corrosion test, and a method for producing the steel sheet, and an automotive component.
[Background Art]
[0002] In recent years, from the viewpoint of global environmental conservation, there has been a strong demand for improving vehicle fuel efficiency. Furthermore, from the viewpoint of collision safety of passengers, there has also been a strong demand for increasing the strength of automotive bodies. To satisfy these demands, by increasing the strength and decreasing the thickness of cold-rolled steel sheets serving as a material for automotive components, both a decrease in weight and an increase in strength of automotive bodies have been actively pursued. Many of automotive components are produced by forming a steel sheet, and thus the steel sheet serving as a material for automotive components needs to have excellent formability in addition to high strength.
[0003] The strength of cold-rolled steel sheets can be increased by various methods. Effective means for increasing the strength without considerably impairing the formability is, for example, a solid-solution strengthening method performed by Si addition. However, if a large amount of Si, in particular, 0.5% or more of Si is added to the cold-rolled steel sheet, it is known that a large amount of SiO2 and a Si-containing oxide such as a Si-Mn composite oxide are formed at an interface between the surface of the steel sheet and oxide scale during slab heating or hot-rolling or during annealing performed after the hot-rolling. This Si-containing oxide considerably degrades the chemical convertibility. Furthermore, if a steel sheet subjected to electrodeposition painting is exposed to a severe corrosive environment such as a salt spray test or a combined cyclic corrosion test in which wetting and drying are repeatedly performed, the coating film readily delaminates, which poses a problem in that the corrosion resistance after coating degrades.
[0004] In view of such problems of Si-containing steel sheets, for example, Patent Literature 1 proposes a high-strength cold-rolled steel sheet in which the Si concentration on the surface of the steel sheet is decreased by heating a slab at a temperature of 1200°C or higher during hot-rolling, performing descaling at high pressure, grinding the surface of the resulting hot-rolled steel sheet using a nylon brush with abrasive grains before pickling, and immersing the steel sheet in a 9% hydrochloric acid tank twice to perform pickling.
[0005] Patent Literature 2 proposes a high-strength cold-rolled steel sheet whose corrosion resistance is improved by controlling the line width of a Si-containing linear oxide observed at a depth of 1 to 10 µm from the steel sheet surface to 300 nm or less.
[0006] Patent Literature 3 proposes a technique for improving the ability to remove oxides by controlling the concentration of iron ions (Fe(II)) in hydrochloric acid to 0.5% to 18%.
[0007] In the high-strength cold-rolled steel sheet described in Patent Literature 1, however, even when the Si concentration on the steel sheet surface is decreased before cold-rolling, a Si-containing oxide is formed on the steel sheet surface due to annealing performed after the cold-rolling. Therefore, the corrosion resistance after coating is not improved.
[0008] In the high-strength cold-rolled steel sheet described in Patent Literature 2, the corrosion resistance is not problematic in a corrosive environment such as a salt spray test specified in JIS Z2371. However, sufficient corrosion resistance after coating is not achieved in a severe corrosive environment such as a hot salt water immersion test or a combined cyclic corrosion test.
[0009] That is, a high-strength cold-rolled steel sheet having excellent corrosion resistance after coating is not obtained only by decreasing the Si concentration on the steel sheet surface after hot-rolling or decreasing the amount of the Si-containing linear oxide.
[0010] In the technique described in Patent Literature 3, SiO2 is insoluble in hydrochloric acid and cannot be removed even when the concentration of iron ions is controlled to 0.5% to 18%.
[0011] To solve the above problems, Patent Literature 4 discloses a technique for improving the chemical convertibility by removing a Si-containing oxide concentrated on the steel sheet surface through an annealing process or the like by pickling and furthermore providing a S-based compound to the surface to improve the reactivity with a chemical conversion treatment liquid.
[0012] Patent Literature 5 discloses a technique in which a P-based compound is provided instead of the S-based compound in Patent Literature 4.
[0013] Moreover, to solve the above problems, Patent Literature 6 discloses the following technique for improving the reactivity with a chemical conversion treatment liquid to improve the chemical convertibility. At the first stage, pickling is performed using an oxidizing acid to remove SiO2. At the following second stage, pickling is performed using a non-oxidizing acid to remove an Fe-based oxide formed during the pickling at the first stage.
[Citation List]
[Patent Literature]
[0014]
[PTL 1] Japanese Unexamined Patent Application Publication No. 2004-204350
[PTL 2] Japanese Unexamined Patent Application Publication No. 2004-244698
[PTL 3] Japanese Unexamined Patent Application Publication No. 64-62485
[PTL 4] Japanese Unexamined Patent Application Publication No. 2007-217743
[PTL 5] Japanese Unexamined Patent Application Publication No. 2007-246951
[PTL 6]: Japanese Unexamined Patent Application Publication No. 2012-132092
[Summary of Invention]
[Technical Problem]
[0015] In recent years, the temperature of a chemical conversion treatment liquid has been decreased to reduce the amount of industrial waste (suppress the generation of sludge) and to reduce the operating cost. Thus, the reactivity of the chemical conversion treatment liquid with a steel sheet has been considerably decreased compared with previous chemical conversion conditions. The decrease in the temperature of the chemical conversion treatment liquid does not pose a problem for plain steel sheets, which have been conventionally used and contain only a small amount of alloy, by improving a surface control technique before the chemical conversion treatment, for example. In a high-strength cold-rolled steel sheet containing a large amount of Si, however, the reactivity with the chemical conversion treatment liquid is considerably decreased because of the influence of a Si-containing oxide formed in a surface layer of the steel sheet in the annealing process. Therefore, the reactivity needs to be improved by taking some measures on the steel sheet. The techniques disclosed in Patent Literature 4 and Patent Literature 5 are effective for conventional plain steel sheets, but do not provide a sufficient improvement effect on the decrease in the temperature of the chemical conversion treatment liquid for the high-strength cold-rolled steel sheet containing a large amount of Si. It has been found that, by applying the technique disclosed in Patent Literature 6 to the above techniques, the decrease in the temperature of the chemical conversion treatment liquid can be overcome even in the high-strength cold-rolled steel sheet containing a large amount of Si. In the technique disclosed in Patent Literature 6, however, when the Fe concentration is low, the pickling rate is low and thus the ability to remove a Si-containing oxide is insufficient. Furthermore, when the Fe concentration is high, an iron-based oxide is unfavorably formed, which degrades the chemical convertibility and also the corrosion resistance after coating.
[0016] In view of the foregoing, it is an object of the present invention to provide a cold-rolled steel sheet having excellent chemical convertibility and high corrosion resistance after coating and a method for producing the steel sheet, and to provide an automotive component.
[Solution to Problem]
[0017] To solve the above problems, the inventors have thoroughly studied a method for improving the reactivity between the steel sheet surface and the chemical conversion treatment liquid by analyzing the surface properties of the steel sheet after annealing in detail. As a result, they have found that it is extremely important to pickle, with a strong acid, a surface of the steel sheet subjected to continuous annealing after cold-rolling to remove a Si-containing oxide layer formed in a surface layer of the steel sheet during annealing and also to reduce the steel sheet surface coverage of an iron-based oxide generated on the steel sheet surface as a result of the pickling with a strong acid. Thus, the present invention has been completed.
[0018] The present invention is based on the above findings, and the gist of the present invention is as follows.
- [1] A method for producing a cold-rolled steel sheet includes performing first pickling
with an acid liquid 1) or an acid liquid 2) below on a steel sheet subjected to continuous
annealing after cold-rolling and performing second pickling with an acid liquid made
of a non-oxidizing acid on the steel sheet:
the acid liquid 1) containing nitric acid and hydrochloric acid, in which the nitric acid has a concentration of more than 50 gram/liter (hereafter referred to as g/L or g/1) to 200 g/L or less, a ratio R1 (hydrochloric acid/nitric acid) of a concentration of the hydrochloric acid to the concentration of the nitric acid is 0.01 to 0.25, and a concentration of iron ions is 3 to 50 g/L, and
the acid liquid 2) containing nitric acid and hydrofluoric acid, in which the nitric acid has a concentration of more than 50 g/L to 200 g/L or less, a ratio R2 (hydrofluoric acid/nitric acid) of a concentration of the hydrofluoric acid to the concentration of the nitric acid is 0.01 to 0.25, and a concentration of iron ions is 3 to 50 g/L.
- [2] In the method for producing a cold-rolled steel sheet according to [1], the first pickling is performed at a temperature of the acid liquid of 20°C to 70°C for 3 to 30 seconds.
- [3] In the method for producing a cold-rolled steel sheet according to [1] or [2], the non-oxidizing acid is at least one of hydrochloric acid, sulfuric acid, phosphoric acid, pyrophosphoric acid, formic acid, acetic acid, citric acid, hydrofluoric acid, and oxalic acid.
- [4] In the method for producing a cold-rolled steel sheet according to any one of [1] to [3], the non-oxidizing acid is any one of hydrochloric acid having a concentration of 0.1 to 50 g/L, sulfuric acid having a concentration of 0.1 to 150 g/L, and a mixed acid containing hydrochloric acid having a concentration of 0.1 to 20 g/L and sulfuric acid having a concentration of 0.1 to 60 g/L.
- [5] In the method for producing a cold-rolled steel sheet according to any one of [1] to [4], the second pickling is performed at a temperature of the acid liquid of 20°C to 70°C for 1 to 30 seconds.
- [6] In the method for producing a cold-rolled steel sheet according to any one of [1] to [5], the cold-rolled steel sheet contains Si in an amount of 0.5 to 3.0 mass%.
- [7] In the method for producing a cold-rolled steel sheet according to any one of [1] to [6], the first pickling and the second pickling are continuously performed.
- [8] A cold-rolled steel sheet is produced by the method according to any one of [1] to [7], wherein a Si-containing oxide layer in a surface layer of the steel sheet is removed and a surface coverage of an iron-based oxide present on a surface of the steel sheet is 40% or less.
- [9] In the cold-rolled steel sheet according to [8], a maximum thickness of the iron-based oxide present on the surface of the steel sheet is 150 nm or less.
- [10] An automotive component uses the cold-rolled steel sheet according to [8] or [9].
[Advantageous Effects of Invention]
[0019] The present invention provides a cold-rolled steel sheet having excellent chemical convertibility and high corrosion resistance after coating. According to the production method of the present invention, a cold-rolled steel sheet having excellent chemical convertibility and high corrosion resistance after coating can be easily and stably produced through a typical cold-rolling process and pickling process by simply adjusting the pickling conditions.
[0020] A cold-rolled steel sheet can be provided which has excellent chemical convertibility even when 0.5% to 3.0% of Si is contained or even when the temperature of a chemical conversion treatment liquid is decreased and which has high corrosion resistance after coating even in a severe corrosive environment such as a hot salt water immersion test or a combined cyclic corrosion test. Accordingly, in the present invention, the chemical convertibility and the corrosion resistance after coating of a high-strength cold-rolled steel sheet having a tensile strength TS of 590 MPa or more and containing a large amount of Si can be considerably improved. Thus, the cold-rolled steel sheet according to the present invention can be suitably used for, for example, high-strength components of automotive bodies.
[Brief Description of Drawings]
[0021]
[Fig. 1] Fig. 1 illustrates backscattered electron images of steel sheet surfaces of cold-rolled steel sheet standard samples No. a and No. b for determining the surface coverage of iron-based oxides.
[fig. 2] Fig. 2 illustrates a histogram showing the number of pixels plotted against gray values of the photographs of the backscattered electron images of the cold-rolled steel sheet standard samples No. a and No. b.
[Fig. 3] Fig. 3 is a photograph obtained by observing, with a transmission electron microscope, a cross-section of a coating on a steel sheet surface after pickling with a non-oxidizing acid.
[Fig. 4] Fig. 4 is a graph showing the analysis result of the iron-based oxide observed in Fig. 3 by energy-dispersive X-ray diffractometry (EDX).
[Fig. 5] Fig. 5 illustrates graphs showing depth profiles of 0, Si, Mn, and Fe on surfaces of test specimens in Table 4-1, the depth profiles being measured by GDS.
[Description of Embodiments]
[0022] Hereafter, the present invention will be described in detail. In the following description, the unit of a content of each element of a steel composition is "mass%", which is simply expressed as "%" unless otherwise specified.
[0023] In an annealing process that uses a continuous annealing furnace and is performed to impart desired microstructure, strength, and workability by recrystallizing a cold-rolled steel sheet, a non-oxidizing gas or a reducing gas is normally used as an atmosphere gas, and the dew point is also strictly controlled. Therefore, in typical cold-rolled steel sheets containing only a small amount of alloy, the oxidation of the steel sheet surface is suppressed. In steel sheets containing 0.5% or more of Si or Mn, however, even when the components of the atmosphere gas and the dew point during annealing are strictly controlled, Si, Mn, or the like, which is more easily oxidized than Fe, is oxidized. As a result, silicon oxide (SiO2) or a Si-containing oxide such as a Si-Mn composite oxide is formed on the steel sheet surface. The composition of such an oxide varies in accordance with the composition of the steel sheet, the annealing atmosphere, or the like, but often varies in accordance with mixed conditions of the composition of the steel sheet and the annealing atmosphere in general. It is known that the Si-containing oxide is formed not only on the steel sheet surface, but also in a steel substrate, which degrades the etching properties of the steel sheet surface in a chemical conversion treatment (zinc phosphate treatment) performed as an underlayer treatment for electrodeposition painting and thus adversely affects the steady formation of a chemical conversion coating.
[0024] In recent years, the temperature of the chemical conversion treatment liquid has been decreased in order to reduce the amount of sludge generated during the chemical conversion treatment and reduce the operating cost. Compared with before, the chemical conversion treatment is performed under conditions in which the reactivity of the chemical conversion treatment liquid with the steel sheet is considerably low. Such a change in chemical conversion conditions does not pose a problem for plain steel sheets, which have been conventionally used and contain only a small amount of alloy, by improving a surface control technique, for example. However, in steel sheets containing a large amount of alloy components, in particular, in high-strength cold-rolled steel sheets whose strength is increased by adding a large amount of Si, the change in the chemical conversion conditions, that is, the decrease in the temperature of the chemical conversion treatment liquid has quite a large influence. Therefore, in cold-rolled steel sheets containing a large amount of Si, the reactivity with the chemical conversion treatment liquid needs to be improved by activating the surface of the steel sheet itself in order to overcome the degradation of chemical conversion conditions.
[0025] The inventors have studied a method for improving the chemical convertibility of the steel sheet to overcome the degradation of chemical conversion conditions described above. As a result, they have found that it is effective to pickle the surface of a cold-rolled steel sheet subjected to continuous annealing using a strong acid such as nitric acid as a pickling solution to remove a Si-containing oxide layer formed in a surface layer of the steel sheet through continuous annealing or the like after cold-rolling. Herein, the Si-containing oxide refers to SiO2 or a Si-Mn composite oxide formed along grain boundaries on the steel sheet surface or in the steel sheet during slab heating or during annealing after hot-rolling or cold-rolling. The thickness of a layer in which such a Si-containing oxide is present varies depending on the composition of the steel sheet and the annealing conditions (temperature, time, and atmosphere), and is normally about 1 µm from the steel sheet surface. The phrase "to remove a Si-containing oxide layer" in the present invention refers to the removal of a Si-containing oxide layer by performing pickling until peaks of Si and O do not appear when the steel sheet surface is analyzed by GDS (glow discharge spectroscopy) in the depth direction.
[0026] The reason for which a strong acid such as nitric acid is used as the pickling solution is as follows. Among Si-containing oxides, a Si-Mn composite oxide easily dissolves in an acid, but SiO2 does not easily dissolve in an acid. Therefore, to remove SiO2, the Si-containing oxide on the steel sheet surface needs to be removed together with the steel substrate.
[0027] However, as a result of studies conducted by the inventors, it has been found that the chemical convertibility is considerably improved by pickling a steel sheet with a strong acid such as nitric acid after continuous annealing to remove a Si-containing oxide layer present on the steel sheet surface, but the chemical convertibility is sometimes not sufficient. The cause thereof has been further studied. Consequently, the following has been additionally found. That is, the Si-based oxide layer is removed by performing pickling with a strong acid such as nitric acid, but Fe eluted from the steel sheet surface as a result of the pickling forms an iron-based oxide, which is different from the Si-based oxide layer. This iron-based oxide is precipitated on the steel sheet surface so as to cover the steel sheet surface, resulting in the degradation of the chemical convertibility.
[0028] The following has also been additionally found. When iron ions (Fe(II) and Fe(III)) are present to some extent in an acid liquid containing nitric acid or the like, the dissolution rate of iron increases and thus the Si-containing oxide layer is effectively removed. When the concentration of iron ions (Fe(II) and Fe(III)) is excessively high, the amount of the iron-based oxide formed increases, which rather degrades the chemical convertibility. The concentration of iron ions in the present invention refers to the total concentration of Fe(II) ions and Fe(III) ions because, in the acid liquid containing nitric acid, which has a strong oxidation power, the eluted Fe(II) ions relatively quickly change to Fe(III) ions by the nitric acid.
[0029] As a result of the above studies, it is important to remove the Si-containing oxide layer present on the steel sheet surface while the generation of the iron-based oxide on the steel sheet surface is suppressed by performing pickling with an acid liquid containing nitric acid or the like and iron ions in an appropriate iron ion concentration.
[0030] As a result of further studies, it has been found that, to reduce the adverse effect on the chemical convertibility, it is important to suppress the generation of the iron-based oxide on the steel sheet surface and to control the surface coverage of the iron-based oxide on the steel sheet surface to 40% or less. It has also been found that the iron-based oxide present on the steel sheet surface can be dissolved and removed by performing pickling with a non-oxidizing acid after the pickling with a strong acid.
[0031] In the present invention, the first pickling is performed using a strong acid to remove the Si-containing oxide layer present on the steel sheet surface while suppressing the generation of the iron-based oxide on the steel sheet surface. Subsequently, the second pickling is performed using a non-oxidizing acid to control the surface coverage of the iron-based oxide present on the steel sheet surface to 40% or less.
[0032] The inventors have also found that when the coverage of the iron-based oxide generated on the steel sheet surface is controlled to 40% or less by pickling and the maximum thickness of the iron-based oxide is controlled to 150 nm or less, the chemical convertibility is further improved and the corrosion resistance is also further improved. They have also found that the maximum thickness of the iron-based oxide is effectively controlled to 150 nm or less by appropriately setting pickling conditions (concentration, temperature, and time) and non-oxidative pickling conditions (acid concentration, temperature, and time).
[0033] The iron-based oxide in the present invention refers to an oxide mainly containing iron at an atomic concentration ratio of 30% or more among elements other than oxygen constituting the oxide. This iron-based oxide is present with an uneven thickness on the steel sheet surface and is different from a natural oxide film present in the form of a layer with a uniform thickness of several nanometers. The iron-based oxide generated on the surface of the cold-rolled steel sheet is found to be amorphous from the observation with a transmission electron microscope (TEM) and the analysis result of a diffraction pattern obtained by electron diffraction analysis.
[0034] The present invention has been completed based on the above new findings and further studies.
[0035] Next, a method for producing a cold-rolled steel sheet according to the present invention will be described.
[0036] In the present invention, for example, a steel sheet obtained by heating a steel material (slab) containing Si in an amount of 0.5% to 3.0% and performing hot-rolling, cold-rolling, and continuous annealing is subjected to first pickling using an acid liquid 1) or an acid liquid 2) below and then subjected to second pickling using an acid liquid made of a non-oxidizing acid.
The acid liquid 1) containing nitric acid and hydrochloric acid, wherein the nitric acid has a concentration of more than 50 g/L and 200 g/L or less, the ratio R1 (hydrochloric acid/nitric acid) of the concentration of the hydrochloric acid to the concentration of the nitric acid is 0.01 to 0.25, and the concentration of iron ions (total of Fe(II) and Fe(III)) is 3 to 50 g/L.
The acid liquid 2) containing nitric acid and hydrofluoric acid, wherein the nitric acid has a concentration of more than 50 g/L and 200 g/L or less, the ratio R2 (hydrofluoric acid/nitric acid) of the concentration of the hydrofluoric acid to the concentration of the nitric acid is 0.01 to 0.25, and the concentration of iron ions (total of Fe(II) and Fe(III)) is 3 to 50 g/L.
[0037] By performing such pickling, the chemical convertibility and the corrosion resistance after coating are considerably improved.
First pickling conditions
[0038] A large amount of Si-containing oxides such as SiO2 and a Si-Mn composite oxide are generated in a surface layer of the steel sheet after continuous annealing. In this state, the chemical convertibility and the corrosion resistance after coating are considerably degraded. In the production method according to the present invention, the first pickling is performed by pickling a cold-rolled steel sheet after annealing using an acid liquid containing nitric acid and hydrochloric acid or an acid liquid containing nitric acid or hydrofluoric acid to remove a Si-containing oxide layer on the steel sheet surface together with the steel substrate.
[0039] Among the Si-containing oxides, the Si-Mn composite oxide easily dissolves in an acid, but the SiO2 does not easily dissolve in an acid. Therefore, to remove the Si-containing oxide including SiO2, an oxide layer needs to be removed together with the steel substrate of the steel sheet by performing pickling with a strong acid. In the present invention, nitric acid, which has a strong oxidation power, is used as an acid for the acid liquid. An acid liquid containing nitric acid and hydrochloric acid or an acid liquid containing nitric acid and hydrofluoric acid is used. It is also effective to add a pickling accelerator to the acid liquid or perform electrolysis in a combined manner to facilitate the dissolution of the steel substrate.
[0040] As described above, Fe eluted from the steel sheet surface by pickling forms an iron-based oxide, and this iron-based oxide is precipitated on the steel sheet surface so as to cover the steel sheet surface. Consequently, the chemical convertibility is sometimes degraded. To prevent this and to reduce the load on the second pickling, the amount of the iron-based oxide generated on the steel sheet surface is preferably suppressed. For the above reasons, the following pickling conditions are specified.
[0041] To effectively remove the Si-containing oxide, when the acid liquid containing nitric acid and hydrochloric acid is used, the concentration of the nitric acid is set to more than 50 g/L and 200 g/L or less. Furthermore, the nitric acid and the hydrochloric acid, which has an effect of breaking an oxide film, are mixed so that the ratio R1 (hydrochloric acid/nitric acid) of the concentration of the hydrochloric acid to the concentration of the nitric acid is 0.01 to 0.25. The concentration of iron ions (total of Fe(II) and Fe(III)) is 3 to 50 g/L. When the acid liquid containing nitric acid and hydrofluoric acid is used, the concentration of the nitric acid is set to more than 50 g/L and 200 g/L or less. Furthermore, the nitric acid and the hydrofluoric acid, which has an effect of breaking an oxide film, are mixed so that the ratio R2 (hydrofluoric acid/nitric acid) of the concentration of the hydrofluoric acid to the concentration of the nitric acid is 0.01 to 0.25. The concentration of iron ions (total of Fe(II) and Fe(III)) is 3 to 50 g/L. If the concentration of the nitric acid is 50 g/L or less, a long time is required for pickling, which increases the facility length and thus increases the facility cost. If the concentration of the nitric acid is more than 200 g/L, the eluted iron is oxidized to generate an iron-based oxide. This iron-based oxide is precipitated on the steel sheet surface, which adversely affects the chemical convertibility and the corrosion resistance after coating. If R1 or R2 is more than 0.25 or the concentration of iron ions (total of Fe(II) and Fe(III)) is less than 3 g/L, a desired pickling rate is not achieved, and thus the Si-containing oxide cannot be efficiently removed. If R1 or R2 is less than 0.01 or the Fe concentration is more than 50 g/L, a desired pickling rate is achieved, but a large amount of iron-based oxide is formed on the steel sheet surface because of a large amount of iron ions in the pickling solution. Thus, the iron-based oxide cannot be completely removed during the second pickling. Consequently, the chemical convertibility and the corrosion resistance cannot be improved.
[0042] Herein, the concentration of iron ions (total of Fe(II) and Fe(III)) is maintained to 3 to 50 g/L by, for example, the following method. When the concentration exceeds 50 g/L, dilution is performed by adding nitric acid and hydrochloric acid. Alternatively, a method for decreasing the amount of iron in an acid using an iron-removing apparatus may be employed.
[0043] Furthermore, the maximum thickness of the iron-based oxide can be controlled to 150 nm or less by appropriately setting the pickling conditions (concentration, temperature, and time). When the first pickling is performed at a temperature of the acid liquid of 20°C to 70°C for 3 to 30 seconds, the maximum thickness of the iron-based oxide is controlled to 150 nm or less. Consequently, the chemical convertibility is further improved, and the corrosion resistance is also further improved.
Second pickling conditions
[0044] The first pickling with a strong acid is not sufficient to stably control the surface coverage of the iron-based oxide generated on the steel sheet surface to 40% or less. In the present invention, therefore, second pickling is performed in order to decrease, with certainty, the amount of the iron-based oxide generated on the steel sheet surface as a result of the first pickling. That is, pickling is performed using an acid liquid made of a non-oxidizing acid to dissolve and remove the iron-based oxide.
[0045] The non-oxidizing acid is at least one of hydrochloric acid, sulfuric acid, phosphoric acid, pyrophosphoric acid, formic acid, acetic acid, citric acid, hydrofluoric acid, and oxalic acid. Any of them may be used, and hydrochloric acid and sulfuric acid commonly used in the iron industry can be preferably used. Among them, hydrochloric acid can be suitably used because hydrochloric acid is a volatile acid and thus a residue such as a sulfate ion is not easily left on the steel sheet surface subjected to washing with water unlike sulfuric acid, and hydrochloric acid has a large effect of breaking an oxide due to a chloride ion. Alternatively, a mixed acid containing hydrochloric acid and sulfuric acid may be used.
[0046] In particular, for the purpose of preventing the degradation of the steel sheet surface quality due to lack of removal of the iron-based oxide and excess pickling, any one of hydrochloric acid having a concentration of 0.1 to 50 g/L, sulfuric acid having a concentration of 0.1 to 150 g/L, and a mixed acid containing hydrochloric acid having a concentration of 0.1 to 20 g/L and sulfuric acid having a concentration of 0.1 to 60 g/L is preferably used.
[0047] The second pickling is preferably performed at a temperature of the acid liquid of 20°C to 70°C for 1 to 30 seconds. When the temperature of the pickling solution is 20°C or higher and the treatment time is 1 second or more, the iron-based oxide left on the steel sheet surface is sufficiently removed. When the temperature of the pickling solution is 70°C or lower and the treatment time is 30 seconds or less, the steel sheet surface is not excessively dissolved and another surface oxide film is not formed.
[0048] To obtain a steel sheet having better chemical convertibility and higher corrosion resistance, the maximum thickness of the iron-based oxide present on the steel sheet surface after the pickling is preferably decreased to 150 nm or less with certainty. To achieve this, the concentration of the acid liquid made of a non-oxidizing acid is preferably increased to an appropriate value. For example, when hydrochloric acid is used, the concentration of the hydrochloric acid is preferably 3 to 50 g/L. When sulfuric acid is used, the concentration of the sulfuric acid is preferably 8 to 150 g/L. When a pickling solution prepared by mixing hydrochloric acid and sulfuric acid is used, a mixed acid containing hydrochloric acid having a concentration of 3 to 20 g/L and sulfuric acid having a concentration of 8 to 60 g/L is preferably used. When the concentration is within the above range, the thickness of the iron-based oxide can be decreased to 150 nm or less with certainty, and thus the chemical convertibility and the corrosion resistance after coating are improved. Furthermore, when the concentration is within the above range, the steel sheet surface is not excessively dissolved and another surface oxide film is not formed.
[0049] As described above, after continuous annealing, the first pickling and the second pickling are performed. Subsequently, an ordinary process such as temper rolling is performed to obtain a product sheet (cold-rolled steel sheet).
[0050] In the present invention, the pickling method, that is, a method for contacting a steel sheet with the acid liquid described in the present invention is not particularly limited. There may be a method for spraying the acid liquid onto a steel sheet or a method for immersing a steel sheet in the acid liquid.
[0051] The first pickling and the second pickling are preferably performed in a continuous manner. This prevents the steel sheet from naturally oxidizing after the first pickling, and an end product can be obtained at a time. Thus, production can be performed at low cost.
[0052] Next, the composition of the cold-rolled steel sheet according to the present invention will be described.
[0053] In the present invention, the cold-rolled steel sheet preferably has such a composition that high strength sufficient for chassis parts and the like of automobiles and good chemical convertibility can be achieved.
[0054] The Si content is preferably 0.5% to 3.0%. Si has a large effect (solid-solution strengthening ability) of increasing the strength of steel without considerably impairing the workability. Therefore, Si is an element effective for increasing the strength of steel, but is also an element that adversely affects the chemical convertibility and the corrosion resistance after coating. For the above reason, the Si content is preferably 0.5% or more. If the Si content is more than 3.0%, the hot rollability and the cold rollability are considerably degraded, which may adversely affect the productivity or degrade the ductility of the steel sheet itself. Accordingly, when Si is added, the Si content is preferably 0.5% to 3.0% and more preferably 0.8% to 2.5%.
[0055] Components other than Si are allowable as long as the contents of the components are within the ranges of typical cold-rolled steel sheets. Herein, when the cold-rolled steel sheet according to the present invention is applied to a high-strength cold-rolled steel sheet having a tensile strength TS of 590 MPa or more and used for automotive bodies and the like, the suitable composition except for Si is preferably as follows.
C: 0.01% to 0.30%
[0056] C is an element effective for increasing the strength of steel and also an element effective for generating retained austenite having a TRIP (transformation induced plasticity) effect, bainite, and martensite. When the C content is 0.01% or more, the above effects are produced. When the C content is 0.30% or less, the weldability does not degrade. Accordingly, the C content is preferably 0.01% to 0.30% and more preferably 0.10% to 0.20%.
Mn: 1.0% to 7.5%
[0057] Mn is an element that increases the strength of steel through solid-solution strengthening, improves the hardenability, and facilitates the generation of retained austenite, bainite, and martensite. When the Mn content is 1.0% or more, such effects are produced. When the Mn content is 7.5% or less, the above effects are produced without increasing the cost. Accordingly, the Mn content is preferably 1.0% to 7.5% and more preferably 2.0% to 5.0%.
P: 0.05% or less
[0058] P is an element that does not degrade the drawability despite its high solid-solution strengthening ability and that is effective for increasing the strength. Therefore, the P content is preferably 0.005% or more. Although P is an element that degrades the spot weldability, no problem is posed when the P content is 0.05% or less. Accordingly, the P content is preferably 0.05% or less and more preferably 0.02% or less.
S: 0.01% or less
[0059] S is an impurity element that unavoidably mixes and a harmful component that precipitates in steel in the form of MnS to degrade the stretch flangeability of the steel sheet. To prevent the degradation of stretch flangeability, the S content is preferably 0.01% or less and more preferably 0.005% or less.
Al: 0.01% to 0.06%
[0060] Al is an element that is added as a deoxidizer in a steelmaking process and that is effective for separating a nonmetal inclusion which degrades the stretch flangeability in the form of slag. Therefore, the Al content is preferably 0.01% or more. When the Al content is 0.06% or less, the above effects can be produced without increasing the raw material cost. Accordingly, the Al content is preferably 0.01% to 0.06% and more preferably 0.02% to 0.06%.
[0061] In the cold-rolled steel sheet according to the present invention, the balance other than the above components is Fe and unavoidable impurities. However, the addition of other components is not necessarily denied as long as the advantageous effects of the present invention are not impaired.
[0062] Next, the surface properties of the cold-rolled steel sheet according to the present invention will be described.
[0063] As described above, the cold-rolled steel sheet according to the present invention has a steel sheet surface from which the Si-containing oxide layer, such as SiO2 and a Si-Mn composite oxide, formed in the surface layer of the steel sheet during annealing has been removed.
[0064] In the cold-rolled steel sheet according to the present invention, in addition to the removal of the Si-containing oxide layer, the surface coverage of the iron-based oxide present on the steel sheet surface needs to be decreased to 40% or less. This is because if the surface coverage is more than 40%, the dissolution reaction of iron in the chemical conversion treatment is inhibited, which suppresses the growth of conversion crystals of zinc phosphate or the like. However, in the case where a chemical conversion treatment liquid whose temperature is decreased is used, a coverage of 40% or less is insufficient for cold-rolled steel sheets used for parts, such as chassis parts of vehicles that severely corrode, required to have very high corrosion resistance after coating. Therefore, the surface coverage needs to be further decreased to 35% or less. The surface coverage is preferably 35% or less.
[0065] In the present invention, the surface coverage of the iron-based oxide is determined by the following method.
[0066] A steel sheet surface subjected to pickling is observed for about five fields at an acceleration voltage of 2 kV at a working distance of 3.0 mm with about 1000-fold magnification using an ultra-low-voltage scanning electron microscope (ULV-SEM) that can detect information regarding an outermost surface layer. Spectroscopic analysis is performed using an energy-dispersive X-ray diffractometer (EDX) to obtain a backscattered electron image. The backscattered electron image is processed using image analysis software such as Image J. Specifically, the backscattered electron image is converted into a binary representation to measure the area fraction of a black portion. By averaging the measured values in the fields, the surface coverage of the iron-based oxide can be obtained. An example of the ultra-low-voltage scanning electron microscope (ULV-SEM) is ULTRA 55 manufactured by SEISS. An example of the energy-dispersive X-ray diffractometer (EDX) is NSS312E manufactured by Thermo Fisher.
[0067] The threshold of the binary conversion will be described. A steel slab shown in Table 1 is subjected to hot-rolling, cold-rolling, and continuous annealing under the conditions shown in Table 2 to obtain a cold-rolled steel sheet having a sheet thickness of 1.8 mm. Subsequently, the cold-rolled steel sheet after the continuous annealing is pickled under the conditions shown in Table 3, washed with water, dried, and then temper-rolled at an elongation percentage of 0.7% to obtain two cold-rolled steel sheets No. a and No. b containing different amounts of iron-based oxides on the steel sheet surfaces. Subsequently, the cold-rolled steel sheet No. a is defined as a standard sample containing a large amount of iron-based oxide, and the cold-rolled steel sheet No. b is defined as a standard sample containing a small amount of iron-based oxide. Each of the steel sheets is observed using a scanning electron microscope under the above conditions to obtain a backscattered electron image. Fig. 1 illustrates photographs of the backscattered electron images of the steel sheets No. a and No. b. Fig. 2 illustrates a histogram showing the number of pixels plotted against gray values of the photographs of the backscattered electron images of the steel sheets No. a and No. b. In the present invention, the gray value (Y point) corresponding to an intersection point (X point) of the histogram No. a and the histogram No. b in Fig. 2 is defined as a threshold. The surface coverages of the iron-based oxides on the steel sheets No. a and No. b were actually determined using the threshold. The surface coverage was 85.3% in the steel sheet No. a and 25.8% in the steel sheet No. b.
[Table 1]
| Chemical composition (mass%) | ||||||
| C | Si | Mn | P | S | Al | Si/Mn |
| 0.14 | 1.65 | 1.33 | 0.018 | 0.002 | 0.035 | 1.24 |
[Table 2]
| No. | Heating temperature (°C) | Hot-rolling conditions | Cold-rolling reduction ratio (%) | Continuous annealing conditions | Strength | |||||||
| Finishing temperature (°C) | Cooling rate (°C/s) | Coiling temperature (°C) | Heating temperature (°C) | Holding time (s) | Coaling rate (°C/s) | Cooling stop temperature (°C) | Holding time (s) | Cooling rate (°C/s) | TS (MPa) | |||
| 1 | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 624 |
[Table 3]
| Steel sheet | First pickling conditions | Second pickling conditions | Surface coverage of iron-based oxide (%) | ||||
| Acid concentration (g/l) | Temperature (°C) | Treatment time (s) | Acid concentration (g/l) | Temperature (°C) | Treatment time (s) | ||
| a | Nitric acid: 250 + Hydrochloric acid: 25 | 40 | 10 | - | - | - | 85.3 |
| b | Nitric acid: 150 + Hydrochloric acid: 15 | 40 | 10 | Hydrochloric acid: 10 | 40 | 30 | 25.8 |
[0068] To further improve the chemical convertibility and also the corrosion resistance, the surface coverage of the iron-based oxide on the steel sheet surface after the second pickling is preferably 40% or less and also the maximum thickness of the iron-based oxide is preferably 150 nm or less. When the maximum thickness of the iron-based oxide is 150 nm or less, the dissolution reaction of iron in the chemical conversion treatment is not locally inhibited, and the precipitation of conversion crystals of zinc phosphate or the like is not locally suppressed. The maximum thickness is more preferably 130 nm or less.
[0070] First, ten extraction replicas that allow the observation of a cross-section having a length of about 8 µm in the width direction of the steel sheet are prepared from the steel sheet surface after the pickling by focused ion beam (FIB) machining. Subsequently, the cross-section (8 µm) of each replica is continuously captured at an acceleration voltage of 200 kV with 100,000-fold magnification using a transmission electron microscope (TEM) equipped with an energy-dispersive X-ray diffractometer (EDX) with which the local information of a cross-section can be investigated.
As one example, Fig. 3 is a photograph obtained by observing, with a transmission electron microscope (TEM), the cross-section of a coating layer generated on the steel sheet surface as a result of the first pickling. Fig. 4 illustrates the EDX analysis result of the coating layer.
As is clear from Fig. 4, the coating layer is found to be formed of an iron-based oxide. The distance between the line A that indicates a steel sheet substrate and the line B that indicates the thickest portion of the iron-based oxide layer in the cross-sectional photograph of Fig. 3 is measured for all the ten replicas. The largest distance is defined as the maximum thickness of the iron-based oxide. Note that the size and number of replicas, the measurement conditions with a TEM, and the like are merely examples, and may be obviously changed appropriately.
[0071] The thus-obtained cold-rolled steel sheet has excellent chemical convertibility and high corrosion resistance after coating evaluated by a hot salt water immersion test or a combined cyclic corrosion test, and therefore can be suitably used for automotive components.
[Example 1]
[0073] A steel containing C: 0.125%, Si: 1.5%, Mn: 2.6%, P: 0.019%, S: 0.008%, and Al: 0.040%, with the balance being Fe and unavoidable impurities, was refined through typical refining processes such as a converter process and degassing and continuously cast to obtain a steel material (slab). Subsequently, the slab was reheated to a temperature of 1150°C to 1170°C, then hot-rolled at a finishing temperature of 850°C to 880°C, and coiled at a temperature of 500°C to 550°C to obtain a hot-rolled steel sheet having a sheet thickness of 3 to 4 mm. Then, the hot-rolled steel sheet was pickled to remove scales and then cold-rolled to obtain a cold-rolled steel sheet having a sheet thickness of 1.8 mm. Then, the cold-rolled steel sheet was subjected to continuous annealing in which the steel sheet was heated to a soaking temperature of 750°C to 780°C and held for 40 to 50 seconds, then cooled from the soaking temperature to a cooling stop temperature of 350°C to 400°C at 20 to 30°C/s, and held in the cooling stop temperature range for 100 to 120 seconds. Subsequently, the steel sheet surface was pickled under the conditions shown in Table 4-1 and Table 4-2, washed with water, dried, and then temper-rolled at an elongation percentage of 0.7% to obtain cold-rolled steel sheets Nos. 2 to 80 in Table 4-1 and Table 4-2.
[0074] A test specimen was collected from each of the cold-rolled steel sheets. The steel sheet surface was observed for five fields at an acceleration voltage of 2 kV at a working distance of 3.0 mm with 1000-fold magnification using an ultra-low-voltage scanning electron microscope (ULV-SEM, manufactured by SEISS, ULTRA 55). Spectroscopic analysis was performed using an energy-dispersive X-ray diffractometer (EDX, manufactured by Thermo Fisher, NSS312E) to obtain a backscattered electron image. The backscattered electron image was processed using image analysis software (Image J). The gray value (Y point) corresponding to an intersection point (X point) of the histograms of the standard samples No. a and No. b described above was defined as a threshold. The backscattered electron image was converted into a binary representation to measure the area fraction of a black portion. The average of the measured values in the five fields was used as the surface coverage of the iron-based oxide.
[0075] Furthermore, a test specimen was collected from each of the cold-rolled steel sheets. The test specimen was subjected to a chemical conversion treatment and a coating treatment under the conditions below and then subjected to three corrosion tests of a hot salt water immersion test, a salt spray test, and a combined cyclic corrosion test. Thus, the corrosion resistance after coating was evaluated. Moreover, the depth profiles of 0, Si, Mn, and Fe were measured by GDS for the surface of the test specimen collected from each of the cold-rolled steel sheets.
(1) Chemical conversion conditions
[0076] The test specimen collected from each of the cold-rolled steel sheets was subjected to a chemical conversion treatment so that the chemical conversion coating had a coating weight of 1.7 to 3.0 g/m2. The chemical conversion treatment was performed using a degreasing agent FC-E2011, a surface controlling agent PL-X, and a chemical conversion treatment agent Palbond PB-L3065 manufactured by Nihon Parkerizing Co., Ltd. under two conditions below which are standard conditions and comparative conditions in which the temperature of the chemical conversion treatment liquid was decreased.
<Standard conditions>
[0077]
- Degreasing process: treatment temperature 40°C, treatment time 120 seconds
- Spray degreasing, surface controlling process: pH 9.5, treatment temperature room temperature, treatment time 20 seconds
- Chemical conversion process: temperature of chemical conversion treatment liquid 35°C, treatment time 120 seconds
<Low-temperature conditions>
[0078] The temperature of the chemical conversion treatment liquid in the standard conditions was decreased to 33°C.
(2) Corrosion test
[0079] Electrodeposition painting was performed on the surface of the test specimen subjected to the above chemical conversion treatment using an electrodeposition paint V-50 manufactured by NIPPONPAINT Co., Ltd. so that a layer having a thickness of 25 µm was formed. The test specimen was subjected to the three corrosion tests below.
<Hot salt water immersion test>
[0080] The surface of the test specimen (n = 1) subjected to the chemical conversion treatment and the electrodeposition painting was cut with a cutter to form a crosscut mark having a length of 45 mm. The test specimen was then immersed in a 5 mass% NaCl solution (60°C) for 360 hours, washed with water, and dried. Subsequently, a tape peel-off test was performed by attaching an adhesive tape to a cut mark portion and then peeling off the adhesive tape. The maximum total width of peeling on both left and right sides of the cut mark portion was measured. When the maximum total width of peeling is 5.0 mm or less, the corrosion resistance in the hot salt water immersion test is evaluated to be good.
<Salt spray test (SST)>
[0081] The surface of the test specimen (n = 1) subjected to the chemical conversion treatment and the electrodeposition painting was cut with a cutter to form a crosscut mark having a length of 45 mm. The test specimen was then subjected to a salt spray test for 1200 hours using a 5 mass% aqueous NaCl solution in conformity with a neutral salt spray test specified in JIS Z2371:2000. Subsequently, a tape peel-off test was performed on a crosscut mark portion. The maximum total width of peeling on both left and right sides of the cut mark portion was measured. When the maximum total width of peeling is 4.0 mm or less, the corrosion resistance in the salt spray test is evaluated to be good.
<Combined cyclic corrosion test (CCT)>
[0082] The surface of the test specimen (n = 1) subjected to the chemical conversion treatment and the electrodeposition painting was cut with a cutter to form a crosscut mark having a length of 45 mm. The test specimen was subjected to a corrosion test in which 120 cycles each including salt spraying (5 mass% aqueous NaCl solution: 35°C, relative humidity: 98%) x 2 hours → drying (60°C, relative humidity: 30%) x 2 hours → wetting (50°C, relative humidity: 95%) x 2 hours were repeatedly performed. The test specimen was washed with water and dried. Subsequently, a tape peel-off test was performed on a cut mark portion. The maximum total width of peeling on both left and right sides of the cut mark portion was measured. When the maximum total width of peeling is 6.0 mm or less, the corrosion resistance in the combined cyclic corrosion test is evaluated to be good.
[0083] Table 4-1 and Table 4-2 show the results of the tests together with the conditions of the tests.
[Table 4-1]
| No. | First pickling conditions | Second pickling conditions | Surface properties | Total width of peeling after corrosion test (mm) | Remarks | |||||||||
| Acid concentration (g/l) | Acid ratio | Concentration of iron ions (g/l) | Temperature | Treatment time | Acid concentration | Temperature | Treatment time | Surface coverage of iron-based oxide (%) | Temperature of chemical conversion treatment liquid | |||||
| R1 (Hydrochloric acid/ Nitric acid) R2 (Hydrofluoric acid/ Nitric acid) | (°C) | (s) | (g/l) | (°C) | (s) | 35°C | 33°C | |||||||
| Hol sait water Immersion test | Sail spray test | Combined cyclic corrosion lest | ||||||||||||
| 2 | Nitric acid 130 + Hydrochloric acid: 15 | R1 = 0.12 | 3.3 | 40 | 10 | - | - | - | 73.1 | 6.4 | 5.6 | 7.9 | 8.4 | Comparative Example |
| 3 | 3.5 | Hydrochloric acid: 0.1 | 40 | 1 | 39.2 | 4.8 | 4.0 | 5.9 | 5.9 | Invention Example | ||||
| 4 | 10 | 36.1 | 4.6 | 3.9 | 5.5 | 5.5 | Invention Example | |||||||
| 5 | 30 | 30.5 | 4.5 | 3.5 | 5.1 | 5.2 | Invention Example | |||||||
| 6 | 3.2 | Hydrochloric acid: 15 | 20 | 1 | 38.9 | 4.8 | 4.0 | 5.8 | 5.7 | Invention Example | ||||
| 7 | 10 | 35.7 | 4.7 | 3.6 | 5.4 | 5.6 | Invention Example | |||||||
| 8 | 30 | 31.5 | 4.6 | 3.5 | 5.3 | 5.2 | Invention Example | |||||||
| 9 | 3.5 | Hydrochloric acid: 15 | 40 | 1 | 34.9 | 4.5 | 3.6 | 5.3 | 5.7 | Invention Example | ||||
| 10 | 10 | 31.0 | 4.5 | 3.6 | 4.9 | 5.2 | Invention Example | |||||||
| 11 | 30 | 25.6 | 4.1 | 3.1 | 4.3 | 4.6 | Invention Example | |||||||
| 12 | 3.9 | Hydrochloric acid: 15 | 70 | 1 | 30.6 | 4.3 | 3.4 | 4.8 | 4.9 | Invention Example | ||||
| 13 | 10 | 25.0 | 4.2 | 3.3 | 4.4 | 4.6 | Invention Example | |||||||
| 14 | 30 | 22.1 | 4.1 | 3.0 | 4.1 | 4.3 | Invention Example | |||||||
| 15 | 3.7 | Hydrochloric acid: 50 | 40 | 1 | 29.2 | 4.2 | 3.4 | 4.8 | 4.7 | Invention Example | ||||
| 16 | 10 | 25.9 | 4.1 | 3.2 | 4.4 | 4.5 | Invention Example | |||||||
| 17 | 30 | 21.9 | 3.9 | 3.0 | 3.9 | 3.9 | Invention Example | |||||||
| 18 | 3.1 | Hydrochloric acid: 75 | 40 | 1 | 37.6 | 4.8 | 4.0 | 5.7 | 5.7 | Invention Example | ||||
| 19 | 10 | 37.1 | 4.7 | 4.0 | 5.7 | 5.8 | Invention Example | |||||||
| 20 | 30 | 36.5 | 4.6 | 3.9 | 5.8 | 5.7 | Invention Example | |||||||
| 21 | Nitric acid: 130 + Hydrofluoric acid: 15 | R2 = 0.12 | 3.7 | 40 | 10 | Hydrochloric acid: 0.1 | 40 | 1 | 37.2 | 4.7 | 3.8 | 5.8 | 5.9 | Invention Example |
| 22 | 10 | 36.5 | 4.6 | 3.6 | 5.8 | 5.9 | Invention Example | |||||||
| 23 | 30 | 35.1 | 4.5 | 3.6 | 5.5 | 5.7 | Invention Example | |||||||
| 24 | 3.9 | Hydrochloric acid: 15 | 20 | 1 | 38.2 | 4.7 | 3.8 | 5.8 | 5.8 | Invention Exampia | ||||
| 25 | 10 | 35.9 | 4.7 | 3.7 | 5.7 | 5.8 | Invention Example | |||||||
| 26 | 30 | 34.3 | 4.6 | 3.7 | 5.7 | 5.7 | Invention Example | |||||||
| 27 | 3.5 | Hydrochloric acid: 15 | 40 | 1 | 35.1 | 4.6 | 3.9 | 5.7 | 5.7 | Invention Example | ||||
| 28 | 10 | 33.3 | 4.6 | 3.7 | 5.7 | 5.7 | Invention Example | |||||||
| 29 | 30 | 31.9 | 4.5 | 3.6 | 5.5 | 5.5 | Invention Example | |||||||
| 30 | 3.6 | Hydrochloric acid: 15 | 70 | 1 | 34.6 | 4.7 | 3.8 | 5.8 | 5.8 | Invention Example | ||||
| 31 | 10 | 34.2 | 4.6 | 3.7 | 5.7 | 5.7 | Invention Example | |||||||
| 32 | 30 | 32.8 | 4.5 | 3.7 | 5.6 | 5.7 | Invention Example | |||||||
| 33 | 3.4 | Hydrochloric acid: 50 | 40 | 1 | 34.5 | 4.6 | 3.9 | 5.7 | 5.8 | Invention Example | ||||
| 34 | 10 | 33.2 | 4.5 | 3.8 | 5.7 | 5.7 | Invention Example | |||||||
| 35 | 30 | 31.5 | 4.5 | 3.8 | 5.7 | 5.7 | Invention Example | |||||||
| 36 | 31 | Hydrochloric acid. 75 | 40 | 1 | 39.5 | 4.7 | 3.9 | 5.9 | 5.8 | Invention Example | ||||
| 37 | 10 | 39.0 | 4.8 | 3.9 | 5.8 | 5.7 | Invention Example | |||||||
| 38 | 30 | 38.3 | 4.5 | 3.8 | 5.8 | 5.6 | Invention Example | |||||||
[Table 4-2]
| No. | First pickling conditions | Second pickling conditions | Surface properties | Total width of peeling after corrosion test (mm) | Remarks | |||||||||
| Acid concentration (g/l) | Acid ratio | Concentration of iron ions (g/l) | Temperature | Treatment time | Acid concentration | temperature | Treatment time | Surface coverage of iron-based oxide | Temperature of chemical treatment liquid | |||||
| R1 (Hydrochloric acid/Nitric acid) R2 (Hydrofluoric acid/Nitric acid) | (°C) | (s) | (g/l) | (°C) | (s) | (%) | 35°C | 33°C | ||||||
| Hot salt waler immersion test | Sail spray test | Combined corrosion | cyclic test | |||||||||||
| 39 | Nitric acid: 130 + Hydrochloric acid: 15 | Rt = 0.12 | 3.1 | 40 | 10 | Sulfuric acid: 0.1 | 40 | 1 | 36.9 | 4.9 | 4.0 | 5.5 | 5.8 | Invention Example |
| 40 | 10 | 36.2 | 4.8 | 3.9 | 5.5 | 5.7 | Invention Example | |||||||
| 41 | 30 | 30.1 | 4.6 | 3.8 | 5.2 | 5.3 | Invention Example | |||||||
| 42 | 3.8 | Sulfuric acid: 50 | 20 | 1 | 39.3 | 4.7 | 4.0 | 5.9 | 5.8 | Invention Example | ||||
| 43 | 10 | 36.7 | 4.7 | 3.9 | 5.6 | 55 | Invention Example | |||||||
| 44 | 30 | 33.3 | 4.6 | 3.8 | 5.1 | 5.3 | Invention Example | |||||||
| 45 | 3.5 | Sulfuric acid: 50 | 40 | 1 | 35.1 | 4.9 | 3.7 | 5.6 | 5.7 | Invention Example | ||||
| 46 | 10 | 30.2 | 4.5 | 3.5 | 5.3 | 5.2 | Invention Example | |||||||
| 47 | 30 | 25.8 | 4.4 | 3.3 | 4.9 | 4.9 | Invention Example | |||||||
| 48 | 3.3 | Sulfuric acid:50 | 70 | 1 | 30.8 | 4.4 | 3.7 | 5.2 | 5.1 | Invention Example | ||||
| 49 | 10 | 25.2 | 4.3 | 3.5 | 4.9 | 4.8 | Invention Example | |||||||
| 50 | 30 | 21.3 | 4.1 | 3.2 | 4.6 | 47 | Invention Example | |||||||
| 51 | 3.5 | Sulfuric acid: 150 | 40 | 1 | 30.2 | 4.9 | 3.6 | 5.1 | 5.1 | Invention Example | ||||
| 52 | 10 | 26.4 | 4.2 | 3.3 | 4.6 | 4.7 | Invention Example | |||||||
| 53 | 30 | 21.6 | 4.3 | 3.2 | 4.3 | 4.6 | Invention Example | |||||||
| 54 | 4.1 | Sulfuric acid: 200 | 40 | 1 | 38.5 | 4.9 | 4.0 | 5.9 | 5.9 | Invention Example | ||||
| 55 | 10 | 38.3 | 4.7 | 3.8 | 5.7 | 5.8 | Invention Example | |||||||
| 56 | 30 | 37.2 | 4.7 | 3.6 | 5.7 | 5.8 | Invention Example | |||||||
| 57 | Nitric acid: 130 + Hydrofluoric acid: 15 | R2 = 0.12 | 3.5 | 40 | 10 | Sulfuric add: 0.1 | 40 | 1 | 36.5 | 4.8 | 4.0 | 5.8 | 5.9 | Invention Example |
| 58 | 10 | 38.3 | 4.7 | 3.9 | 5.7 | 5.6 | Invention Example | |||||||
| 59 | 30 | 38.0 | 4.7 | 3.9 | 5.7 | 5.8 | Invention Example | |||||||
| 60 | 4.3 | Sulfuric acid: 50 | 20 | 1 | 37.2 | 4.8 | 3.8 | 5.8 | 6.9 | Invention Example | ||||
| 61 | 10 | 37.1 | 4.7 | 3.8 | 5.7 | 5.9 | Invention Example | |||||||
| 82 | 30 | 36.5 | 4.6 | 3.7 | 5.6 | 5.8 | Invention Example | |||||||
| 63 | 4.2 | Sulfuric acid: 50 | 40 | 1 | 36.1 | 4.9 | 3.9 | 5.8 | 5.8 | Invention Example | ||||
| 64 | 10 | 35.7 | 4.7 | 3.8 | 5.8 | 5.8 | Invention Example | |||||||
| 65 | 30 | 35.5 | 4.6 | 3.7 | 5.7 | 5.7 | Invention Example | |||||||
| 66 | 3.4 | Sulfuric acid. 50 | 70 | 1 | 35.1 | 4.8 | 3.8 | 5.7 | 5.9 | Invention Example | ||||
| 67 | 10 | 34.8 | 4.8 | 3.8 | 5.6 | 5.7 | Invention Example | |||||||
| 68 | 30 | 34.5 | 4.6 | 3.7 | 5.6 | 5.7 | Invention Example | |||||||
| 69 | 3.1 | Sulfuric acid: 150 | 40 | 1 | 33.2 | 4.7 | 3.8 | 5.7 | 5.8 | Invention Example | ||||
| 70 | 10 | 33.1 | 4.7 | 3.7 | 5.6 | 5.8 | Invention Example | |||||||
| 71 | 30 | 32.5 | 4.6 | 3.7 | 5.5 | 5.5 | Invention Example | |||||||
| 72 | 3.8 | Sulfuric acid: 200 | 40 | 1 | 39.3 | 4.6 | 4.0 | 5.9 | 5.9 | Invention Example | ||||
| 73 | 10 | 39.1 | 4.8 | 4.0 | 5.9 | 5.8 | Invention Example | |||||||
| 74 | 30 | 38.8 | 4.7 | 3.9 | 5.6 | 5.7 | Invention Example | |||||||
| 75 | Nitric acid: 130 + Hydrochloric acid: 15 | R1 = 0.12 | 3.2 | 40 | 10 | Hydrochloric acid: 10 +Sulfuric acid: 10 | 40 | 1 | 35.4 | 4.3 | 3.9 | 5.5 | 5.7 | Invention Example |
| 76 | 10 | 30.5 | 4.2 | 3.7 | 5.0 | 5.0 | Invention Example | |||||||
| 77 | 30 | 26.2 | 4.1 | 3.3 | 47 | 4.7 | Invention Example | |||||||
| 78 | Nitric acid: sdd: 130 + Hydrochloric acid: 15 | R1 = 0.12 | 3.9 | 40 | 10 | Hydrochloric acid: 20 + Sulfuric acid: 50 | 40 | 1 | 33.4 | 4.3 | 3.7 | 5.2 | 5.8 | Invention Example |
| 79 | 10 | 30.7 | 4.2 | 3.5 | 4.9 | 5.2 | Invention Example | |||||||
| 80 | 30 | 25.6 | 3.9 | 3.4 | 4.6 | 4.7 | Invention Example | |||||||
[0084] As is clear from Table 4-1 and Table 4-2, the steel sheets of Invention Examples that were pickled under the conditions of the present invention after continuous annealing had a small maximum total width of peeling in any of the hot salt water immersion test, the salt spray test, and the combined cyclic corrosion test. Thus, the steel sheets of Invention Examples had excellent chemical convertibility and high corrosion resistance after coating. In particular, all the cold-rolled steel sheets having a surface coverage of the iron-based oxide of 40% or less had excellent corrosion resistance after coating in a severe corrosive environment. The depth profiles of O, Si, Mn, and Fe on each of the steel sheet surfaces in Table 4-1 and Table 4-2 were measured by GDS. It was confirmed that peaks of Si and 0 did not appear for the steel sheets pickled under the conditions of the present invention, and thus the Si-containing oxide layer was sufficiently removed. For reference, Fig. 5 illustrates depth profiles of O, Si, Mn, and Fe obtained when the test specimen No. 2 of Comparative Example and the test specimen No. 9 of Invention Example in Table 4-1 were subjected to surface analysis by GDS.
[Example 2]
[0085] Steels A to O having compositions shown in Table 5 were refined through typical refining processes such as a converter process and degassing and continuously cast to obtain steel slabs. Each of the steel slabs was hot-rolled under the hot-rolling conditions shown in Table 6 to obtain a hot-rolled steel sheet having a sheet thickness of 3 to 4 mm. The hot-rolled steel sheet was pickled to remove scales on the steel sheet surface and then cold-rolled to obtain a cold-rolled steel sheet having a sheet thickness of 1.8 mm. Subsequently, the cold-rolled steel sheet was subjected to continuous annealing and pickling under the conditions shown in Tables 6 and 7, then washed with water, dried, and temper-rolled at an elongation percentage of 0.7% to obtain each of cold-rolled steel sheets Nos. 81 to 111.
[0086] A test specimen was collected from each of the thus-obtained cold-rolled steel sheets. The surface coverage of the iron-based oxide on the steel sheet surface after pickling was measured in the same manner as in Example 1. Then, the test specimen was subjected to a tensile test and a test for corrosion resistance after coating described below. Furthermore, the depth profiles of O, Si, Mn, and Fe on the surface of the test specimen collected from each of the cold-rolled steel sheets were measured by GDS.
(1) Mechanical properties
[0087] A tensile test was performed in conformity with JIS Z2241:1998 using a JIS No. 5 tensile test specimen (n = 1) specified in JIS Z2201:1998 and collected in a direction (C direction) perpendicular to the rolling direction. Thus, the tensile strength TS was measured.
(2) Corrosion resistance after coating
[0088] A test specimen collected from each of the cold-rolled steel sheets was subjected to a chemical conversion treatment and electrodeposition painting under the same conditions as in Example 1. The test specimen was subjected to three corrosion tests of a hot salt water immersion test, a salt spray test (SST), and a combined cyclic corrosion test (CCT) in the same manner as in Example 1. Thus, the corrosion resistance after coating was evaluated.
[0089] Table 7 shows the results of the tests (the tensile strength TS is shown in Table 6).
[Table 5]
| Steel Symbol | Chemical composition (mass%) | Si/Mn | |||||
| C | Si | Mn | P | S | Al | ||
| A | 0.11 | 1.25 | 1.55 | 0.018 | 0.001 | 0.032 | 0.81 |
| B | 0.15 | 1.30 | 1.80 | 0.019 | 0.002 | 0.033 | 0.72 |
| C | 0.15 | 1.20 | 1.95 | 0.017 | 0.001 | 0.033 | 0.62 |
| D | 0.09 | 1.45 | 1.40 | 0.017 | 0.002 | 0.028 | 1.04 |
| E | 0.18 | 1.11 | 1.36 | 0.018 | 0.001 | 0.032 | 0.82 |
| F | 0.16 | 1.41 | 1.23 | 0.017 | 0.001 | 0.041 | 1.15 |
| G | 0.14 | 1.65 | 1.33 | 0.018 | 0.002 | 0.035 | 1.24 |
| H | 0.12 | 1.45 | 2.10 | 0.017 | 0.001 | 0.042 | 0.69 |
| I | 0.17 | 0.90 | 1.40 | 0.017 | 0.002 | 0.044 | 0.64 |
| J | 0.13 | 1.20 | 1.89 | 0.018 | 0.001 | 0.041 | 0.63 |
| K | 0.15 | 1.20 | 1.85 | 0.017 | 0.001 | 0.034 | 0.65 |
| L | 0.03 | 1.25 | 3.25 | 0.018 | 0.001 | 0.005 | 0.38 |
| M | 0.22 | 3.30 | 1.15 | 0.018 | 0.001 | 0.027 | 2.87 |
| O | 0.11 | 0.45 | 1.50 | 0.020 | 0.003 | 0.030 | 0.30 |
[Table 6]
| No. | Steel | Heating temperature (°C) | Hot-rolling conditions | Cold-rolling | Continuous annealing conditions | Tensile strength TS (MPa) | |||||||
| Symbol | Finishing temperature (°C) | Cooling rate (°C/s) | Coiling temperature (°C) | Reduction ratio (%) | Heating temperature (°C) | Holding time (s) | Cooling rate (°C/s) | Cooling stop temperature (°C) | Holding time (s) | Cooling rate (°C/s) | |||
| 81 | A | 1150 | 850 | 25 | 620 | 60 | 780 | 45 | 20 | 350 | 100 | 40 | 623 |
| 82 | B | 1150 | 820 | 31 | 400 | 60 | 780 | 40 | 20 | 400 | 100 | 50 | 822 |
| 83 | C | 1150 | 820 | 31 | 400 | 60 | 780 | 40 | 20 | 400 | 100 | 50 | 821 |
| 84 | D | 1140 | 850 | 26 | 600 | 60 | 760 | 50 | 20 | 350 | 100 | 45 | 816 |
| 85 | E | 1150 | 840 | 33 | 530 | 60 | 730 | 40 | 20 | 350 | 110 | 40 | 625 |
| 86 | F | 1150 | 850 | 30 | 580 | 55 | 750 | 35 | 20 | 400 | 110 | 50 | 833 |
| 87 | G | 1150 | 850 | 25 | 620 | 60 | 750 | 50 | 20 | 350 | 120 | 50 | 631 |
| 88 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 635 |
| 89 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 633 |
| 90 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 633 |
| 91 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 632 |
| 92 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 635 |
| 93 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 639 |
| 94 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 636 |
| 95 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 632 |
| 96 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 634 |
| 97 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 631 |
| 98 | G | 1150 | 850 | 33 | 550 | 60 | 750 | 30 | 20 | 400 | 100 | 50 | 634 |
| 99 | H | 1130 | 820 | 28 | 570 | 60 | 780 | 50 | 15 | 370 | 150 | 50 | 838 |
| 100 | I | 1150 | 840 | 34 | 530 | 55 | 780 | 50 | 15 | 350 | 120 | 55 | 821 |
| 101 | J | 1140 | 850 | 28 | 600 | 60 | 770 | 60 | 20 | 300 | 100 | 45 | 835 |
| 102 | K | 1150 | 850 | 25 | 620 | 60 | 780 | 45 | 20 | 350 | 100 | 40 | 649 |
| 103 | L | 1100 | 850 | 33 | 550 | 60 | 750 | 50 | 20 | 450 | 150 | 50 | 958 |
| 104 | L | 1100 | 850 | 33 | 550 | 60 | 750 | 50 | 20 | 450 | 150 | 50 | 957 |
| 105 | L | 1100 | 850 | 33 | 550 | 60 | 750 | 50 | 20 | 450 | 150 | 50 | 961 |
| 106 | L | 1100 | 850 | 33 | 550 | 60 | 750 | 50 | 20 | 450 | 150 | 50 | 961 |
| 107 | L | 1100 | 850 | 33 | 550 | 60 | 750 | 50 | 20 | 450 | 150 | 50 | 962 |
| 108 | M | 1120 | 830 | 31 | 550 | 55 | 720 | 50 | 15 | 410 | 190 | 50 | 1131 |
| 109 | O | 990 | 690 | 25 | 540 | 75 | 750 | 35 | 20 | 400 | 100 | 50 | 754 |
| 110 | O | 970 | 710 | 28 | 540 | 70 | 750 | 35 | 20 | 400 | 100 | 50 | 793 |
| 111 | O | 960 | 700 | 27 | 550 | 75 | 750 | 35 | I 20 | 400 | 100 | 50 | 805 |
[Table 7]
| No. | Steel | First pickling conditions | Second pickling conditions | Surface properties | Total width of peeling after corrosion test (mm) | Remarks | |||||||||
| Symbol | Acid concentration (g/l) | Acid ratio | Concentration of iron Ions (g/l) | Temperature | Treatment time | Acid concentration (g/l) | Temperature | Treatment time | Surface coverage of iron based oxide | Temperature of chemical conversion treatment liquid: 35°C | 33°C | ||||
| Rt (Hydrochloric acid/Nitric acid) R2 (Hydrafluoric acid/Nitric acid) | (°C) | (s) | (°C) | (s) | (%) | Hot salt water immersion test | Salt spray test | Combined cyclic corrosion test | |||||||
| 81 | A | Nitric acid: 130 + Chloric acid: 15 | R1 =0.12 | 5.9 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 31.5 | 4.3 | 3.8 | 4.6 | 4.7 | Invention Example |
| 82 | B | 32.3 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 38.3 | 4.7 | 3.9 | 4.9 | 4.8 | Invention Example | ||
| 83 | C | Nitric acid: 130 + Chloric acid: 15 | R1 =0.12 | 6.2 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 31.2 | 4.4 | 3.5 | 4.6 | 5.1 | Invention Example |
| 84 | O | 6.1 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 30.5 | 4.3 | 3.9 | 4.8 | 5.2 | Invention Example | ||
| 85 | E | 7.3 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 30.1 | 4.2 | 3.9 | 4.7 | 5.1 | Invention Example | ||
| 86 | F | 8.2 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 30.3 | 4.4 | 3.6 | 4.8 | 5.1 | Invention Example | ||
| 87 | G | 5.9 | 40 | 10 | Chloric acid: 10 | 10 | 1 | 33.2 | 4.8 | 3.9 | 4.7 | 5.2 | Invention Example | ||
| 88 | G | 6.9 | 40 | 10 | Chloric acid: 10 | 40 | 1 | 34.3 | 4.4 | 3.9 | 5.1 | 5.4 | Invention Example | ||
| 89 | G | 6.8 | 40 | 10 | Chloric acid: 10 | 40 | 30 | 26.9 | 4.2 | 3.1 | 4.4 | 4.5 | Invention Example | ||
| 90 | G | 53.2 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 52.9 | 5.9 | 4.9 | 7.5 | 7.6 | Comparative Example | ||
| 91 | G | 4.9 | 40 | 10 | Sulfuric acid: 75 | 40 | 30 | 26.7 | 4.1 | 3.2 | 4.7 | 4.8 | Invention Example | ||
| 92 | G | 5.8 | 40 | 10 | Chloric acid: 100 | 40 | 10 | 31.3 | 4.5 | 3.8 | 5.2 | 5.5 | Invention Example | ||
| 93 | G | Nitric acid: 130 + Hydrofluoric acid: 15 | R2 = 0.12 | 4.2 | 40 | 10 | Chloric acid: 10 | 10 | 33.3 | 4.4 | 3.8 | 5.1 | 5.4 | Invention Example | |
| 94 | G | 4.5 | 40 | 10 | Chloric acid: 10 | 40 | 1 | 33.2 | 4.3 | 4 | 5 | 5.3 | Invention Example | ||
| 95 | G | 6.3 | 40 | 10 | Chloric acid: 10 | 40 | 30 | 27.8 | 4.3 | 3.3 | 4.3 | 4.5 | Invention Example | ||
| 96 | G | 52.1 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 53.9 | 5.9 | 5.8 | 7.4 | 7.5 | Comparative Example | ||
| 97 | G | 7.2 | 40 | 10 | Sulfuric acid: 75 | 40 | 30 | 26.5 | 4.1 | 3.9 | 4.5 | 4.7 | Invention Example | ||
| 98 | G | 5.8 | 40 | 10 | Chloric acid: 100 | 40 | 10 | 31.5 | 4.5 | 3.9 | 5.3 | 5.6 | Invention Example | ||
| 99 | H | Nitric acid: 130 + Chloric acid: 15 | R1 = 0.12 | 11.1 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 35.1 | 4.5 | 3.9 | 4.7 | 5.3 | Invention Example |
| 100 | I | 9.2 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 31.5 | 4.4 | 3.9 | 4.9 | 5.5 | Invention Example | ||
| 101 | J | 8.3 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 31.3 | 4.5 | 3.9 | 4.8 | 5.3 | Invention Example | ||
| 102 | K | 6.6 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 30.5 | 4.2 | 3.9 | 4.6 | 5.3 | Invention Example | ||
| 103 | L | 5.9 | 40 | 10 | Sulfuric acid: 75 | 10 | 1 | 32.9 | 4.4 | 3.7 | 4.7 | 5.5 | Invention Example | ||
| 104 | L | 13.5 | 40 | 10 | Sulfuric acid: 75 | 40 | 1 | 36.2 | 4.4 | 3.9 | 5.2 | 5.5 | Invention Example | ||
| 105 | L | 12.1 | 40 | 10 | Sulfuric acid: 75 | 40 | 30 | 29.8 | 4.2 | 3.5 | 4.8 | 5.6 | Invention Example | ||
| 106 | L | 3 | 40 | 10 | Chloric acid: 10 | 40 | 30 | 26.1 | 4.5 | 3.1 | 5.2 | 5.3 | Invention Example | ||
| 107 | L | 4.5 | 40 | 10 | Sulfuric acid: 200 | 40 | 10 | 32.5 | 4.3 | 3.8 | 5.3 | 5.5 | Invention Example | ||
| 108 | M | 5.2 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 32.6 | 4.3 | 3.7 | 5.1 | 5.4 | Invention Example | ||
| 109 | N | Nitric acid : 100 +Chloric acid : 5 | R1=0.05 | 23.1 | 40 | 10 | Chloric acid : 10 | 40 | 10 | 29.9 | 4.3 | 3.7 | 4.9 | 5.2 | Invention Example |
| 110 | N | 15.2 | 40 | 10 | Chloric acid : 10 | 40 | 10 | 30.5 | 4.4 | 3.7 | 4.9 | 5.3 | Invention Example | ||
| 111 | N | Nitric acid 150 +Chloric acid : 15 | R1=0.10 | 36 | 40 | 10 | Chloric acid : 10 | 40 | 10 | 31.2 | 4.2 | 3.6 | 4.6 | 5.2 | Invention Example |
| 109 | O | Nitric acid: 100 + Chloric acid: 5 | R1=0.05 | 4.6 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 35.3 | 4.4 | 3.9 | 5.2 | 5.3 | Invention Example |
| 110 | O | 4.8 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 36.2 | 4.3 | 3.9 | 5.2 | 5.3 | Invention Example | ||
| 111 | O | Nitric acid· 150 + Chloric acid: 15 | R1=0.10 | 6.2 | 40 | 10 | Chloric acid: 10 | 40 | 10 | 30.2 | 4.2 | 3.8 | 4.9 | 5.2 | Invention Example |
[0090] As is clear from Table 6 and Table 7, the high-strength cold-rolled steel sheets of Invention Examples that contained 0.5% or more of Si and pickled under the conditions of the present invention to decrease the surface coverage of the iron-based oxide on the steel sheet surface to 40% or less had not only excellent chemical convertibility and high corrosion resistance after coating, but also high strength with a tensile strength TS of 590 MPa or more. The depth profiles of 0, Si, Mn, and Fe were measured by GDS. It was confirmed that peaks of Si and O did not appear for all the steel sheets pickled under the conditions of the present invention, and thus the Si-containing oxide layer was sufficiently removed.
[Example 3]
[0091] A steel containing C: 0.125%, Si: 1.5%, Mn: 2.6%, P: 0.019%, S: 0.008%, and Al: 0.040%, with the balance being Fe and unavoidable impurities, was refined and continuously cast to obtain a steel material (slab). The slab was reheated to a temperature of 1150°C to 1170°C, then hot-rolled at a finishing temperature of 850°C to 880°C, and coiled at a temperature of 500°C to 550°C to obtain a hot-rolled steel sheet having a sheet thickness of 3 to 4 mm. The hot-rolled steel sheet was pickled to remove scales and then cold-rolled to obtain a cold-rolled steel sheet having a sheet thickness of 1.8 mm. Then, the cold-rolled steel sheet was subjected to continuous annealing in which the steel sheet was heated to a soaking temperature of 750°C to 780°C and held for 40 to 50 seconds, then cooled from the soaking temperature to a cooling stop temperature of 350°C to 400°C at 20 to 30°C/s, and held in the cooling stop temperature range for 100 to 120 seconds. Subsequently, the steel sheet surface was pickled under the conditions shown in Table 8, washed with water, dried, and then temper-rolled at an elongation percentage of 0.7% to obtain cold-rolled steel sheets Nos. 112 to 149 in Table 8.
[0092] A test specimen was collected from each of the cold-rolled steel sheets. The surface coverage and maximum thickness of the iron-based oxide generated on the steel sheet surface as a result of the pickling were measured by the above-described methods.
[0093] Furthermore, a test specimen was collected from each of the cold-rolled steel sheets. The test specimen was subjected to a chemical conversion treatment and a coating treatment under the conditions below and then subjected to three corrosion tests of a hot salt water immersion test, a salt spray test, and a combined cyclic corrosion test. Thus, the corrosion resistance after coating was evaluated. Moreover, the depth profiles of O, Si, Mn, and Fe were measured by GDS for the surface of the test specimen collected from each of the cold-rolled steel sheets.
(1) Chemical conversion conditions
[0094] The test specimen collected from each of the cold-rolled steel sheets was subjected to a chemical conversion treatment so that the chemical conversion coating had a coating weight of 1.7 to 3.0 g/m2. The chemical conversion treatment was performed using a degreasing agent FC-E2011, a surface controlling agent PL-X, and a chemical conversion treatment agent Palbond PB-L3065 manufactured by Nihon Parkerizing Co., Ltd. under two conditions below which are standard conditions and comparative conditions in which the temperature of the chemical conversion treatment liquid was decreased.
<Standard conditions>
[0095]
- Degreasing process: treatment temperature 40°C, treatment time 120 seconds
- Spray degreasing, surface controlling process: pH 9.5, treatment temperature room temperature, treatment time 20 seconds
- Chemical conversion process: temperature of chemical conversion treatment liquid 35°C, treatment time 120 seconds
<Low-temperature conditions>
[0096] The temperature of the chemical conversion treatment liquid in the standard conditions was decreased to 33°C.
(2) Corrosion test
[0097] Electrodeposition painting was performed on the surface of the test specimen subjected to the above chemical conversion treatment using an electrodeposition paint V-50 manufactured by NIPPONPAINT Co., Ltd. so that a layer having a thickness of 25 µm was formed. The test specimen was subjected to the three corrosion tests below under more strict conditions than those of Example 1.
<Hot salt water immersion test>
[0098] The surface of the test specimen (n = 1) subjected to the chemical conversion treatment and the electrodeposition painting was cut with a cutter to form a crosscut mark having a length of 45 mm. The test specimen was then immersed in a 5 mass% NaCl solution (60°C) for 480 hours, washed with water, and dried. Subsequently, a tape peel-off test was performed by attaching an adhesive tape to a cut mark portion and then peeling off the adhesive tape. The maximum total width of peeling on both left and right sides of the cut mark portion was measured. When the maximum total width of peeling is 5.0 mm or less, the corrosion resistance in the hot salt water immersion test is evaluated to be good.
<Salt spray test (SST)>
[0099] The surface of the test specimen (n = 1) subjected to the chemical conversion treatment and the electrodeposition painting was cut with a cutter to form a crosscut mark having a length of 45 mm. The test specimen was then subjected to a salt spray test for 1400 hours using a 5 mass% aqueous NaCl solution in conformity with a neutral salt spray test specified in JIS Z2371:2000. Subsequently, a tape peel-off test was performed on a crosscut mark portion. The maximum total width of peeling on both left and right sides of the cut mark portion was measured. When the maximum total width of peeling is 4.0 mm or less, the corrosion resistance in the salt spray test is evaluated to be good.
<Combined cyclic corrosion test (CCT)>
[0100] The surface of the test specimen (n = 1) subjected to the chemical conversion treatment and the electrodeposition painting was cut with a cutter to form a crosscut mark having a length of 45 mm. The test specimen was subjected to a corrosion test in which 150 cycles each including salt spraying (5 mass% aqueous NaCl solution: 35°C, relative humidity: 98%) x 2 hours → drying (60°C, relative humidity: 30%) x 2 hours → wetting (50°C, relative humidity: 95%) x 2 hours were repeatedly performed. The test specimen was washed with water and dried. Subsequently, a tape peel-off test was performed on a cut mark portion. The maximum total width of peeling on both left and right sides of the cut mark portion was measured. When the maximum total width of peeling is 6.0 mm or less, the corrosion resistance in the combined cyclic corrosion test is evaluated to be good.
[0101] Table 8 shows the results of the tests.
[Table 8]
| No. | First pickling conditions | Second pickling conditions | Surface properties | Total width of peeling after corrosion lest (mm) | Remarks | ||||||||||
| Acid concentration (g/l) | Acid ratio | Concentration of iron ions | Temperature | Treatment time | Acid concentration | Temperature | Treatment time | Surface coverage of iron-based oxide (%) | Maximum thickness of iron based oxide (nm) | Temperature of chemical conversion treatment liquid: 35°C | 33°C | ||||
| R1 (Hydrochloric acid/Nitric acid) R2 (Hydrofluoric acid/Nitric acid) | (g/l) | (°C) | (s) | (g/l) | (°C) | (s) | Hot salt water immersion test | Salt spray test | Combined cyclic corrosion lest | ||||||
| 112 | Nitric acid: 130 * Chloric acid: 15 | R1 = 0.12 | 5.2 | 40 | 10 | - | - | - | 73.2 | 214 | 8.5 | 5.8 | 8.2 | 8.4 | Comparative Example |
| 113 | 6.4 | 40 | 10 | Chloric acid: 0.1 | 40 | 1 | 39.4 | 158 | 5.0 | 4.0 | 6.0 | 5.9 | Invention Example | ||
| 114 | 3.8 | 10 | 36.1 | 158 | 4.9 | 4.0 | 5.9 | 6.0 | Invention Example | ||||||
| 115 | 7.2 | 30 | 31.1 | 158 | 4.9 | 3.9 | 5.9 | 6.0 | Invention Example | ||||||
| 116 | 5.5 | 40 | 10 | Chloric acid. 15 | 40 | 1 | 38.5 | 144 | 4.9 | 3.9 | 5.9 | 5.9 | Invention Example | ||
| 117 | 3.2 | 10 | 32.5 | 139 | 4.8 | 3.9 | 5.7 | 5.7 | Invention Example | ||||||
| 118 | 12.1 | 10 | 34.3 | 142 | 4.9 | 4.0 | 5.9 | 6.0 | Invention Example | ||||||
| 119 | 25.3 | 10 | 35.2 | 145 | 4.8 | 3.9 | 5.8 | 5.9 | Invention Example | ||||||
| 120 | 40.3 | 10 | 36.1 | 148 | 4.9 | 4.0 | 5.9 | 5.9 | Invention Example | ||||||
| 121 | 52.1 | 10 | 45.3 | 172 | 6.2 | 6.2 | 8.1 | 6.3 | Comparative Example | ||||||
| 122 | 3.2 | 30 | 28.2 | 144 | 4.8 | 4.0 | 5.7 | 5.9 | Invention Example | ||||||
| 123 | 5.8 | 40 | 10 | Chloric acid. 50 | 40 | 1 | 30.3 | 93 | 4.3 | 3.6 | 5.1 | 5.3 | Invention Example | ||
| 124 | 3.8 | 10 | 27.1 | 69 | 4.2 | 3.4 | 4.9 | 5.2 | Invention Example | ||||||
| 125 | 10.1 | 30 | 21.5 | 85 | 4.0 | 3.1 | 4.7 | 4.9 | Invention Example | ||||||
| 126 | Nitric acid: 130 + Hydrofluoric acid: +- | R2 = 0.12 | 3.5 | 40 | 10 | Chloric acid: 0.1 | 40 | 1 | 38.3 | 148 | 4.9 | 4.0 | 5.6 | 5.9 | Invention Example |
| 127 | 4.2 | 10 | 35.2 | 147 | 4.8 | 4.0 | 5.7 | 6.0 | Invention Example | ||||||
| 128 | 6.9 | 30 | 30.5 | 145 | 4.3 | 3.8 | 5.5 | 5.8 | Invention Example | ||||||
| 129 | 3.3 | Chloric acid. 50 | 40 | 1 | 37.2 | 95 | 4.5 | 4.0 | 5.0 | 5.6 | Invention Example | ||||
| 130 | 4.5 | 10 | 34.5 | 67 | 4.5 | 3.9 | 4.9 | 5.5 | Invention Example | ||||||
| 131 | 5.3 | 30 | 29.8 | 80 | 4.3 | 3.7 | 4.9 | 5.3 | Invention Example | ||||||
| 132 | 5.6 | Chloric acid: 150 | 40 | 1 | 36.5 | 83 | 4.3 | 4.0 | 4.8 | 5.2 | Invention Example | ||||
| 133 | 8.2 | 10 | 32.5 | 80 | 4.1 | 3.5 | 4.7 | 5.2 | Invention Example | ||||||
| 134 | 5.8 | 30 | 28.5 | 78 | 4.0 | 3.1 | 4.6 | 5.0 | Invention Example | ||||||
| 135 | Nitric acid: 130 + Chloric acid 15 | R1 = 0.12 | 7.5 | 40 | 10 | Sulfuric acid: 0.1 | 40 | 1 | 39.2 | 149 | 4.9 | 3.9 | 5.9 | 5.9 | Invention Example |
| 136 | 3.5 | 10 | 35.1 | 145 | 4.8 | 4.0 | 5.8 | 6.0 | Invention Example | ||||||
| 137 | 6.2 | 30 | 30.3 | 141 | 4.8 | 4.0 | 5.9 | 6.0 | Invention Example | ||||||
| 138 | 6.7 | Sulfuric acid: 50 | 40 | 1 | 37.5 | 148 | 4.8 | 3.9 | 5.9 | 6.0 | Invention Example | ||||
| 139 | 9.1 | 10 | 32.1 | 144 | 4.8 | 3.9 | 5.8 | 5.7 | Invention Example | ||||||
| 140 | 8.2 | 30 | 28.6 | 139 | 4.7 | 3.7 | 5.6 | 5.8 | Invention Example | ||||||
| 141 | 7.5 | Sulfuric acid: 150 | 40 | 1 | 30.5 | 92 | 4.3 | 3.9 | 5.7 | 5.5 | Invention Example | ||||
| 142 | 6.3 | 10 | 26.9 | 88 | 4.3 | 3.6 | 5.5 | 5.3 | Invention Example | ||||||
| 143 | 3.3 | 30 | 24.3 | 85 | 4.1 | 3.3 | 5.2 | 5.1 | Invention Example | ||||||
| 144 | Nitric acid: aCid: 130 + Chloric acid: 15 | R1 = 0.12 | 6.2 | 40 | 10 | Chloric acid 10 + Sulfuric acid: 10 | 40 | 1 | 35.2 | 149 | 4.9 | 3.9 | 5.8 | 5.9 | Invention Example |
| 145 | 5.8 | 10 | 31.5 | 146 | 4.9 | 3.9 | 5.9 | 6.0 | Invention Example | ||||||
| 146 | 6.6 | 30 | 29.3 | 143 | 4.8 | 4.0 | 5.7 | 6.0 | Invention Example | ||||||
| 147 | Nitric acid: 130 + Chloric acid 15 | R1 = 0.12 | 5.7 | 40 | 10 | Chloric acid 20 + Sulfuric acid: 50 | 40 | 1 | 33.3 | 148 | 4.7 | 3.9 | 5.9 | 6.0 | Invention Example |
| 148 | 5.1 | 10 | 29.2 | 145 | 4.8 | 3.8 | 5.8 | 5.7 | Invention Example | ||||||
| 149 | 9.2 | 30 | 26.1 | 142 | 4.8 | 3.8 | 5.7 | 5.8 | Invention Example | ||||||
[0102] As is clear from Table 8, the steel sheets of Invention Examples in which the steel sheet surface after annealing was pickled so that the surface coverage of the iron-based oxide on the steel sheet surface after the second pickling was 40% or less and the maximum thickness of the iron-based oxide was 150 nm or less had a small maximum total width of peeling in any of the hot salt water immersion test, the salt spray test, and the combined cyclic corrosion test performed under strict conditions in which the test time was longer than that in Example 1. Thus, the steel sheets of Invention Examples had very high corrosion resistance after coating. The depth profiles of 0, Si, Mn, and Fe were measured by GDS. It was confirmed that peaks of Si and O did not appear for all the steel sheets pickled under the conditions of the present invention, and thus the Si-containing oxide layer was sufficiently removed.
[Industrial Applicability]
[0103] The cold-rolled steel sheet produced in the present invention is capable of having not only excellent chemical convertibility and high corrosion resistance after coating, but also high strength. The steel sheet can be suitably used as a material for automotive components and also a material for parts required to have the same characteristics in the field of household appliances, building, and the like.
1. A method for producing a cold-rolled steel sheet, comprising:
the acid liquid 2) containing nitric acid and hydrofluoric acid, wherein the nitric acid has a concentration of more than 50 g/L to 200 g/L or less, a ratio R2 (hydrofluoric acid/nitric acid) of a concentration of the hydrofluoric acid to the concentration of the nitric acid is 0.01 to 0.25, and a concentration of iron ions is 3 to 50 g/L.
performing first pickling with an acid liquid 1) or an acid liquid 2) below on a steel sheet subjected to continuous annealing after cold-rolling; and
performing second pickling with an acid liquid made of a non-oxidizing acid on the steel sheet,
the acid liquid 1) containing nitric acid and hydrochloric acid, wherein the nitric acid has a concentration of more than 50 g/L to 200 g/L or less, a ratio R1 (hydrochloric acid/nitric acid) of a concentration of the hydrochloric acid to the concentration of the nitric acid is 0.01 to 0.25, and a concentration of iron ions is 3 to 50 g/L, andthe acid liquid 2) containing nitric acid and hydrofluoric acid, wherein the nitric acid has a concentration of more than 50 g/L to 200 g/L or less, a ratio R2 (hydrofluoric acid/nitric acid) of a concentration of the hydrofluoric acid to the concentration of the nitric acid is 0.01 to 0.25, and a concentration of iron ions is 3 to 50 g/L.
2. The method for producing a cold-rolled steel sheet according to Claim 1, wherein the
first pickling is performed at a temperature of the acid liquid of 20°C to 70°C for
3 to 30 seconds.
3. The method for producing a cold-rolled steel sheet according to Claim 1 or 2, wherein
the non-oxidizing acid is at least one of hydrochloric acid, sulfuric acid, phosphoric
acid, pyrophosphoric acid, formic acid, acetic acid, citric acid, hydrofluoric acid,
and oxalic acid.
4. The method for producing a cold-rolled steel sheet according to any one of Claims
1 to 3, wherein the non-oxidizing acid is any one of hydrochloric acid having a concentration
of 0.1 to 50 g/L, sulfuric acid having a concentration of 0.1 to 150 g/L, and a mixed
acid containing hydrochloric acid having a concentration of 0.1 to 20 g/L and sulfuric
acid having a concentration of 0.1 to 60 g/L.
5. The method for producing a cold-rolled steel sheet according to any one of Claims
1 to 4, wherein the second pickling is performed at a temperature of the acid liquid
of 20°C to 70°C for 1 to 30 seconds.
6. The method for producing a cold-rolled steel sheet according to any one of Claims
1 to 5, wherein the cold-rolled steel sheet contains Si in an amount of 0.5 to 3.0
mass%.
7. The method for producing a cold-rolled steel sheet according to any one of Claims
1 to 6, wherein the first pickling and the second pickling are continuously performed.
8. A cold-rolled steel sheet produced by the method according to any one of Claims 1
to 7, wherein a Si-containing oxide layer in a surface layer of the steel sheet is
removed and a surface coverage of an iron-based oxide present on a surface of the
steel sheet is 40% or less.
9. The cold-rolled steel sheet according to Claim 8, wherein a maximum thickness of the
iron-based oxide present on the surface of the steel sheet is 150 nm or less.
10. An automotive component using the cold-rolled steel sheet according to Claim 8 or
9.
REFERENCES CITED IN THE DESCRIPTION
This list of references cited by the applicant is for the reader's convenience only. It does not form part of the European patent document. Even though great care has been taken in compiling the references, errors or omissions cannot be excluded and the EPO disclaims all liability in this regard.
Patent documents cited in the description
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