KR101359098B1 - High speed pickling process for austenitic stainless cold strip - Google Patents

Abstract

The present invention relates to a method of pickling the surface of a steel plate at high speed when the austenitic cold-rolled stainless steel plate requiring high surface quality is manufactured and more specifically, to a method of pickling a high-chrome austenitic cold-rolled stainless steel plate capable of pickling the austenitic cold-rolled stainless steel plate containing 16 wt.% or more of chrome. The method of pickling a high-chrome austenitic cold-rolled stainless steel plate removes silicon oxide from the cold-rolled steel plate by immersing the cold-rolled steel plate in a mixed acid solution composed of 110-150 g/l of sulfuric acid, 15-25 g/l of free hydrofluoric acid, and 4.5 g/l or more of hydrogen peroxide; wherein the hydrogen peroxide does not contain iron ion. When the austenitic cold-rolled stainless steel plate is pickled, the present invention does not use nitrogen; thereby reducing the installation burden of a de-NOx system. Furthermore, the present invention is appropriate to high-speed production because it can be easily controlled by controlling the pickling process depending on the concentration of the hydrogen peroxide and the hydrofluoric acid and can produce the high quality of the austenitic cold-rolled stainless steel plate because the quality after the pickling process is increased more than the existing pickling process. [Reference numerals] (AA) Concentration of available hydrogen peroxide (g/L); (BB) Concentration of iron ions (g/L)

Description

High Speed Pickling Process for Austenitic Stainless Cold Strip}

The present invention relates to a method of pickling a surface of a steel sheet at high speed in manufacturing an austenitic stainless steel cold rolled steel sheet requiring surface quality, and more particularly, to a pickling method that does not use nitric acid during a pickling process.

The austenitic stainless steel cold rolled steel sheet undergoes a heat treatment of 1000 to 1150 ° C. in order to obtain predetermined mechanical properties after cold rolling. During the heat treatment, the surface of the steel sheet reacts with high temperature oxygen to oxidize to the surface of the steel sheet. Scale (SiO ₂ , (Cr, Mn) ₃ O ₄ ) is produced. Such an oxidized scale produced on the surface of the steel sheet deteriorates the appearance of the product, deteriorates the quality of the steel sheet, and also becomes a starting point that causes corrosion of the steel sheet, thereby lowering the corrosion resistance of the steel sheet.

Therefore, in order to obtain beautiful surface quality and improve corrosion resistance, physical descaling by brush, shotball blasting, etc., electrolytic descaling using sodium sulfate, sulfuric acid, nitric acid electrolyte, chemical descaling using salt bath, mixed acid, etc. Stainless steel cold rolled steel sheet is manufactured by combining the various methods and removing the oxide scale of the steel plate surface.

The process of removing the scaling of such a steel plate surface is called a pickling process. In this stainless steel pickling process, in order to obtain beautiful surface quality and to form a passivation film evenly to secure corrosion resistance, a nitric acid electrolysis method of descaling by applying a current through a steel sheet to a nitric acid solution and nitric acid (80 to 180 g / l) ) And a pickling process by a chemical descaling method using a mixed acid of hydrofluoric acid (2-40 g / l). At this time, the nitric acid in the electrolytic bath lowers the pH in the pickling bath to increase the activity of hydrofluoric acid, and oxidizes the divalent iron ions dissolved at the surface of the steel sheet to trivalent to maintain the redox potential appropriate for the pickling bath.

However, as nitric acid is used as the pickling solution, NOx, an air emission control substance, is generated, and nitrate nitrogen (NO ₃ -N) is included in the waste acid and the wash water. For this reason, in order to satisfy environmental regulatory conditions such as total nitrogen restriction of discharged effluent and NOx concentration restriction of air discharge facilities due to strengthening domestic and foreign environmental regulations, additional costs and installation of environmental pollution prevention facilities in pickling process are incurred. This causes a problem that the production cost is significantly increased.

In order to solve this problem, a pickling method has been developed that does not use nitric acid, and this technique replaces nitric acid with hydrochloric acid or sulfuric acid in the pickling process, and insufficient oxidizing power is hydrogen peroxide, potassium permanganate, trivalent iron ion and air injection. A pickling method has been developed that does not use nitric acid, which is supplemented by.

Specifically, German Patent No. 3937438 discloses a technique of using sulfuric acid, hydrofluoric acid, and iron sulfate as the pickling solution, and adding hydrogen peroxide to maintain the redox potential of the pickling solution at 300 mV or more. Since the 1960s, as disclosed in US Pat. No. 5,477,448 and European Patent No. 236354, techniques that specify the proper range of Oxidation-Reduction Potential (ORP) of mainly hydrofluoric acid and iron ions, air, hydrogen peroxide or solutions It appeared continuously. However, most of these methods have a limitation in that they can be applied to products such as wire rods, steel bars and thick plates, which are not demanding in quality.

On the other hand, U. S. Patent No. 5908511 contains sulfuric acid, hydrofluoric acid, iron salts, and hydrogen peroxide is regularly added, and the pickling is controlled by adjusting the composition of the wetting agent, the brightening agent, the corrosion inhibitor, and the like. A technique that takes an automatic control scheme as the reduction potential (ORP) is disclosed. Through this, CLEANOX352, a pickling solution, has been commercialized and is the most widely used worldwide. This method is used for wire rod and hot rolled products, but the production cost is over 20% higher than the existing one, and it adopts complicated solution composition and management method.

In addition, European Patent Application Publication No. 1040211 and US Patent Application Publication No. 2000-560982 have been proposed to improve the pickling rate by adding copper and chlorine ions to the pickling composition. If the open circuit potential (OCP) formed on the surface of the stainless steel sheet is lower than 0.1 V, which is a redox potential of copper ions, copper particles may precipitate on the surface of the steel sheet and cause discoloration of the steel sheet. There is also a risk of pitting corrosion if the pickling solution contains more than a certain concentration of chlorine ions.

As described above, various techniques are known for the pickling composition, but there is no known pickling technique suitable for producing a high chromium austenitic cold rolled steel sheet at high speed.

The present invention provides an electrolytic pickling method suitable for high-speed production of austenitic stainless steel cold rolled steel sheet and a mixed acid pickling method for removing silicon oxide at high speed without securing nitric acid.

In addition, the present invention is to provide a mixed acid solution containing no nitric acid suitable for the pickling method.

Furthermore, the present invention is to provide an austenitic stainless steel cold rolled steel sheet having a gloss of 150 or more measured at a 60 ° reflection angle in the rolling direction obtained through the pickling method as described above.

The present invention provides a pickling method for rapidly removing silicon oxide from the surface of an austenitic stainless steel cold rolled steel sheet using a mixed acid solution containing no nitric acid.

It does not contain nitric acid, its initial composition is immersed in cold-rolled steel in a mixed acid solution containing 110-150 g / l sulfuric acid, 15-25 g / l free hydrofluoric acid, and 4.5 g / l or more hydrogen peroxide concentration and substantially no iron ions. It provides a method for pickling a high chromium austenitic stainless steel cold rolled steel sheet thereby removing silicon oxide from the cold rolled steel sheet.

The hydrogen peroxide concentration satisfies the following formula (1) in relation to the iron ion concentration, and the redox potential of the solution satisfies the following formula (2) or (3) in relation to the iron ion concentration.

Hydrogen peroxide concentration (g / l) ≥ 0.00736 + 10 × e- ^{[metal] /13.2} (1)

ORP ≥ 600 mV, provided that [metal] ≤ 10 g / l (2)

ORP (mV) ≥ 310 + 431 × e- ^{[metal] /25.24} , where [metal]> 10g / l (3)

In the formulas (1) to (3), [metal] represents the iron ion concentration in the mixed acid solution.

In addition, the surface potential of the cold rolled steel sheet immersed in the mixed acid solution is preferably maintained at -0.2 to 0.1V.

The cold rolled steel sheet is preferably immersed in the mixed acid solution for 10 to 100 seconds.

And, the removal of silicon oxide from the cold rolled steel sheet is carried out after the neutral salt electrolytic treatment step and sulfuric acid electrolytic treatment step, the neutral salt electrolytic treatment step using a Cr-rich scale from the surface of the steel sheet using an electrolytic solution containing sodium sulfate electrolyte Electrolytic removal, the sulfuric acid electrolytic treatment step is to electrolytically remove the residual scale of Cr and Fe using an electrolytic solution containing sulfuric acid as an electrolyte.

At this time, the neutral salt electrolytic treatment step is immersed austenitic stainless steel sheet in a neutral salt electrolytic solution of 50 ~ 90 ℃ temperature, 10 ~ 30A / dm ² so that the potential of the surface of the steel sheet is formed in the order of +,-, + This can be done by applying a current density of 30 seconds to 120 seconds.

In addition, it is preferable to include 100-250 g / l sodium sulfate electrolyte in the neutral salt electrolyte solution.

Further, the sulfuric acid electrolytic treatment step is to immerse the austenitic stainless steel sheet subjected to the neutral salt electrolytic treatment step in sulfuric acid electrolytic solution at a temperature of 30 ~ 60 ℃, 10 ~ so that the potential of the surface of the steel sheet is formed in the order +,-, + This can be done by applying a current density of 30 A / dm ² for 5 seconds to 50 seconds.

The sulfuric acid electrolytic solution preferably contains 50-150 g / l sulfuric acid.

Furthermore, the present invention relates to a high chromium austenitic stainless steel cold rolled steel sheet obtained by the above method, to provide a high chromium austenitic stainless steel cold rolled steel sheet having a gloss of 150 or more measured at an angle of 60 ° in the rolling direction of the cold rolled steel sheet. do.

The present invention also relates to a mixed acid solution for removing silicon oxide from a high chromium austenitic stainless steel cold rolled sheet containing 16 wt% or more of chromium after degreasing and annealing. / l, free hydrofluoric acid 15-25g / l and hydrogen peroxide, the hydrogen peroxide concentration satisfies the following formula (1) in relation to the iron ions in the mixed acid solution, the redox potential (ORP) is iron ions in the mixed acid solution A mixed acid solution for removing silicon oxide from a high chromium austenitic stainless steel cold rolled sheet satisfying the following formula (2) or (3) in relation to the concentration is provided.

Hydrogen peroxide concentration (g / l) ≥ 0.00736 + 10 × e- ^{[metal] /13.2} (1)

ORP ≥ 600mV, where [metal] ≤ 10g / l (2)

ORP (mV) ≥ 310 + 431 × e- ^{[metal] /25.24} , where [metal]> 10g / l (3)

In the formulas (1) to (3), [metal] represents the iron ion concentration in the mixed acid solution.

According to the present invention, in pickling an austenitic stainless steel cold rolled steel sheet, since the mixed acid solution in the pickling solution does not contain nitric acid, NOx and nitric acid nitrogen are not discharged. Therefore, the burden on the installation of a NOx removal installation and a denitration installation can be reduced.

In addition, the pickling can be adjusted by the concentration of hydrogen peroxide, the redox potential (ORP) of the solution and the concentration of hydrofluoric acid, so that it is easy to control and is suitable for high-speed production.

In addition, the quality after pickling is also improved compared to the existing pickling method, it is possible to produce a high quality austenitic stainless steel cold rolled steel sheet.

In addition, by completely removing the Fe and Cr oxides except the silicon oxide in the electrolytic pickling process, it is possible to easily remove the silicon oxide by the mixed acid solution, and to remove and planarize the silicon oxide by the mixed acid solution in 10 to 100 seconds. It can be done in a short time.

In addition, the solution composition is simple, the management method is simple, and the surface quality of the cold rolled steel sheet can be secured by preventing any reaction other than pickling reaction with the surface of the steel sheet, and the productivity can be improved by high speed production. Can be.

1 is an electron micrograph of the surface of the heat-treated high chromium austenitic stainless steel cold rolled steel sheet, A) is an electron microscope photograph of the cross section of the steel plate after the electrolytic treatment, B) is performed electrolytic treatment It is an electron microscope photograph of the cross section of the steel sheet which is not.
2 is a photograph taken with an electron microscope of the surface of a high chromium austenitic stainless steel cold rolled steel sheet pickled in accordance with Example 2, A) is the surface of the steel sheet obtained in Example 4, B) is in Comparative Example 4 It is a steel plate surface obtained by.
3 is a graph showing the correlation between the minimum hydrogen peroxide concentration according to the metal content and the redox potential of the solution in order to maintain the surface potential of -0.2 ~ 0.1V when the high chromium austenitic stainless steel cold rolled steel sheet is immersed in mixed acid to be.

One embodiment of the present invention is a neutral salt electrolytic cell using an austenitic stainless steel cold rolled steel sheet as sodium sulfate, a sulfuric acid electrolytic cell using sulfuric acid and metal sulfate as an electrolyte, and a mixed acid tank of sulfuric acid, hydrogen peroxide and hydrofluoric acid Provided is a method for removing the oxidative scale of the steel sheet surface by passing through. In addition, as another embodiment of the present invention, there is provided a high chromium austenitic stainless cold rolled steel sheet obtained by the method of the present invention. Furthermore, the present invention as another embodiment, to provide a mixed acid solution used to remove the scale of oxidation.

Hereinafter, the present invention will be described in detail.

In general, an austenitic stainless steel cold rolled steel sheet has an oxide scale having a thickness of 200 to 500 nm after heat treatment, and the oxide scale has a Cr-rich scale layer, an oxide scale, and a base material of Cr having a relatively higher Cr oxide scale content than Fe. It has a multilayer structure of the Si-oxide layer which exists in an interface.

Of these scales, the Cr-rich scale layer can be removed in a neutral salt electrolyzer. The neutral salt electrolyzer comprises a neutral salt electrolyte containing a sodium sulfate electrolyte and includes an electrode bath for conducting a current to the surface of the steel sheet. In this case, the electrode assembly is configured such that the potential of the surface of the steel sheet is charged at least one or more times in the order of +,-, +.

The neutral salt electrolyte is preferably in the range of pH 3 to 6, when a current is applied to the neutral salt electrolyte having such a pH range, Cr of the Cr-rich scale layer is preferentially dissolved in the state of Cr ^{6 +} , Cr on the surface of the Cr-rich scale can be removed. At this time, it is preferable to use sodium sulfate as the electrolyte in the neutral salt electrolyte. The sodium sulfate electrolyte causes dissolution of Cr on the Cr-rich scale by increasing the electrical conductivity in the electrolyte to increase the current carrying rate to the steel sheet surface.

At this time, the neutral salt electrolyte is preferably included in the content of sodium sulfate electrolyte 100 to 250g / l. When the sodium sulfate electrolyte is 100g / l or more, an appropriate conductivity for dissolving chromium can be obtained. However, when it exceeds 250 g / l, sodium sulfate precipitates in electrolyte solution, which may block facility piping and worsen operation. Therefore, it is preferable to include sodium sulfate electrolyte at 250 g / l or less.

The electrical conductivity of the electrolyte in the neutral salt electrolyzer is closely related to the temperature of the electrolyte. When the temperature of the electrolyte is 50 ° C. or more, an appropriate conductivity for dissolving chromium in the Cr-rich scale layer may be obtained. The higher the temperature of the electrolyte, the higher the conductivity. However, when the temperature of electrolyte solution exceeds 90 degreeC, temperature management is difficult in operation. Therefore, it is preferable that the temperature of the electrolyte solution in a neutral salt electrolytic cell is 50-90 degreeC.

On the other hand, the current applied through the electrode is preferably 10 A / dm 2 or more. When the current applied through the electrode is 10A / dm ² or more, Cr-rich scale Cr can be sufficiently eluted. However, if it exceeds 30A / dm 2 has a disadvantage that the rectifier (rectifier) equipment for generating a current is enlarged to increase the initial equipment cost, the current is preferably in the range of 10-30A / dm 2.

The treatment time of the neutral salt electrolytic treatment is preferably carried out for 30 seconds to 120 seconds. The descaling effect of chromium can be sufficiently obtained by treating in a neutral salt electrolyzer for the time in the above range. However, when the neutral salt electrolytic treatment time exceeds 120 seconds, there is no further descaling effect, and the metal ions eluted during electrolytic pickling may be electrodeposited again, which is not preferable.

On the other hand, residual scales such as Cr and Fe which are not completely removed in the neutral salt electrolyzer are removed by the sulfuric acid electrolyzer. The sulfuric acid electrolytic cell includes a sulfuric acid electrolytic solution composed of sulfuric acid and a metal sulfate including at least one of iron, chromium, nickel, copper, manganese, and titanium, and an electrode bath for conducting a current to the surface of the steel sheet. The electric potential of the steel plate surface is configured to be charged at least once in the order of +,-, +.

The sulfuric acid electrolyte is preferably in the range pH 0 ~ 1, when a current is applied to such a sulfuric acid electrolytic solution, and is dissolved in the Fe ions of Fe ^{2 +.} At this time, H ⁺ and SO ₄ ^{2 -} in sulfuric acid increase the electrical conductivity in the solution to increase the electrical conductivity from the electrode to the surface of the steel sheet, and additionally lower the pH to chemically dissolve the residual scale iron.

At this time, the sulfuric acid electrolyte solution preferably contains sulfuric acid in the range of 50 to 150g / l. Sulfuric acid should be more than 50g / l to maintain more than the appropriate conductivity, and thus can maintain the current through the surface of the steel sheet. However, when the sulfuric acid exceeds 150g / l, chemical dissolution is predominantly generated, causing a problem that the surface of the stainless steel cold rolled steel sheet is rough.

In addition, the sulfuric acid electrolyte may include a metal sulfate containing at least one of iron, chromium, nickel, copper, manganese, titanium. When the metal sulfate is low in electrical conductivity due to the low metal concentration through the equilibrium reaction, the metal is eluted from the sulfate to increase the electrical conductivity, and when the high metal concentration is high electrical conductivity, it is precipitated as sulfate again to lower the electrical conductivity of the sulfate electrolyte. Make sure the conductivity is kept constant.

Like the electrolyte solution of the neutral salt electrolyzer, the sulfuric acid electrolyte solution preferably has a solution temperature of 30 ° C. or more in order to obtain minimum conductivity. However, when the solution temperature of the sulfuric acid electrolyte exceeds 60 ℃ chemical dissolution proceeds excessively, the surface of the stainless steel cold rolled steel sheet may be rough, and further black smut phenomenon may occur that the steel sheet surface is black. Therefore, it is preferable that the electrolyte solution of the sulfuric acid electrolyzer has a temperature in the range of 30 to 60 ° C.

On the other hand, the current applied to the sulfuric acid electrolyzer is preferably in the range of 10 to 30 A / dm 2. When a current is applied to 10 A / dm 2 or more, the scale elution amount by the electrochemical reaction becomes sufficient, and sufficient electrolytic pickling effect can be obtained. However, when a current exceeding 30 A / dm 2 is applied, there is a disadvantage in that a rectifier facility for generating a current is increased and an initial installation cost is increased. The current is preferably in the range of 10 to 30 A / dm 2.

Such sulfuric acid electrolytic treatment is preferably performed for 5 to 50 seconds. Sulfuric acid electrolytic treatment must be performed for at least 5 seconds to fully descale. However, when the sulfuric acid electrolytic treatment time is more than 50 seconds, it causes a problem of peracid tax, it is preferable to carry out in the above range.

As described above, the surface of the steel plate subjected to the neutral salt electrolysis-sulfuric acid electrolysis is left with a Si oxide layer and a chromium depleted layer in the base material, and the Si oxide layer and the chromium depleted layer can be removed by a mixed acid solution containing no nitrogen. . The mixed acid solution contains sulfuric acid, free hydrofluoric acid, and hydrogen peroxide, and the Si oxide layer from the steel plate subjected to neutral salt electrolysis-sulfuric acid electrolysis by immersing the steel plate including the Si oxide layer and the chromium depleted layer in a mixed acid bath containing the mixed acid solution. And chromium depleted layer can be removed.

Free hydrofluoric acid and sulfuric acid in the mixed acid solution are dissociated in the mixed acid solution as shown in the following reaction formulas (1) and (2).

^{HF ⇔ H + + F - (} 1)

^{_{H 2 SO 4 ⇔ HSO 4 -}} + H + ⇔ SO 4 2 - + 2H + (2)

That is, in the mixed acid solution, free hydrofluoric acid dissociates while dissolving as in formula (1), and sulfuric acid dissociates as in formula (2). At this time, the equilibrium state of the mixed acid solution is changed by H + concentration, that is, acidity, provided by dissociation of the free hydrofluoric acid and sulfuric acid.

In the case of free hydrofluoric acid, it has a pickling force in the undissociated free hydrofluoric acid (Free HF) state to dissolve Si oxide on the surface of the steel sheet, and further, penetrates the interface between the Si oxide layer and the base metal to dissolve Fe. Thus dissolved Fe and Si ions are removed from the steel sheet surface in the form of FeF _x ^(3-x) , H ₂ SiF ₆ and the like.

The free hydrofluoric acid is preferably present in a mixed acid solution at a concentration in the range of 10-30 g / l, more preferably 15-25 g / l. If the concentration of hydrofluoric acid is less than 10 g / l, the concentration of free hydrofluoric acid is small, so that there is a lack of dissolving power in the Si and chromium depleted layers, which may cause fine pickling problems on the surface of the steel sheet, which exceeds 30 g / l. In this case, the erosion rate of the base material may be increased to roughen the surface of the steel sheet after the pickling process.

As described above, since the free hydrofluoric acid provides pickling force for removing the Si oxide layer on the surface of the steel sheet, it is preferable that the effective free hydrofluoric acid concentration is maintained in the mixed acid solution above a certain acidity. Therefore, sulfuric acid of a certain concentration is required in the mixed acid solution to prevent free hydrofluoric acid from dissociating and to dissolve the chromium depleted layer of the base material and to remove the Si oxide generated at the grain boundary. Suitable sulfuric acid concentrations range from 110 to 150 g / l. If the sulfuric acid concentration is less than 110g / l, it is difficult to sufficiently dissolve the chromium depleted layer and grain boundaries of the austenitic steel base material may cause a problem of corrosion resistance after pickling, and if it exceeds 150g / l, heat generation occurs during sulfuric acid dilution operation There is a problem such that operation becomes difficult, and it is preferable to include sulfuric acid at a concentration in the above range.

In the oxide scale of the austenitic stainless steel, Si oxide is present at both the austenitic crystal surface and the grain boundary, and the grain Si oxide is present at a deeper position inside the base material. In the case of ferritic stainless steel, since the corrosion resistance of the crystal is low, there is no difference in the rate of erosion between the inside of the crystal and the grain, so that the grain surface and the grain boundary are completely dissolved without selectivity. do. Therefore, in order to remove all the Si oxides, a large portion of grain boundaries need to be dissolved.

In this case, the Fe ^{2 +} is eluted from the base material, the eluted Fe ^{2 +} is generated by a complex as FeF ^{_{x (3-x),}} in combination with HF after the reaction with the hydrogen peroxide oxidation to Fe ³⁺ is removed from the surface of the steel sheet . Such a reaction can be expressed as the following reaction formulas (3) to (6), it is possible to increase the pickling rate if such a process proceeds smoothly.

^{Fe 0 ⇔ Fe 2 + + 2e} - (3)

^{_{Fe 2 + + H 2 O 2}} → Fe 3 + + · H + OH - (4)

Fe ^{3 +} + 3HF ⇔ FeF ₃ + 3H ⁺ (5)

Cu ^{2 +} + 2e ^- ? Cu ⁰ (6)

The present invention is to implement a high pickling rate by controlling the surface potential of the austenitic stainless steel cold rolled steel sheet in the mixed acid tank, for this purpose to maintain the surface potential of the cold rolled steel sheet in the mixed acid tank in the range of -0.2 to 0.1V It is preferable. If the surface potential of the cold rolled steel sheet is out of the above range, pickling may not occur, or may cause pickling failure with a partially pickled surface. In addition, even if it is pickled, the cold rolled steel sheet cannot obtain good surface quality.

On the other hand, it is conventional to conduct pickling, by controlling the oxidation-reduction potential (ORP) of the tax acid by adjusting the ratio of the Fe ^{2 +} / Fe ^{3 +} of the acid washing. However, the present inventors confirmed that until the metal concentration reached an appropriate level, the relationship between the redox potential (ORP) and the surface potential of the solution could not be confirmed, and therefore, the acid pickling cannot be controlled by the redox potential (ORP) alone. It was.

If the residual hydrogen peroxide concentration is insufficient before the metal concentration in the mixed acid solution reaches an appropriate level, the surface potential of the cold rolled steel sheet in the mixed acid tank will not maintain more than -2.0 V, and thus the reaction of reaction formula (4) As a result, the Fe ²⁺ concentration on the surface of the steel sheet is increased locally, and the reaction in the left direction of the reaction formula (3) predominates. In this case, Cu, which is present as an additive or impurity in Fe and stainless steel, is reprecipitated on the surface of the steel sheet as in Scheme (6), and a blackening phenomenon occurs in which the surface of the steel sheet becomes black. Therefore, the residual hydrogen peroxide concentration always needs to be present above a certain concentration.

However, after the metal concentration in the mixed acid solution reaches an appropriate level, the residual hydrogen peroxide concentration for maintaining a surface potential of -0.2 V or more is correlated with the metal concentration in the solution. That is, the metal concentration in the solution is increased according to the progress of the pickling, the eluted hydrogen peroxide by the Fe ^{+ 2} ion is oxidized to Fe ^{+ 3} ions. The increase in Fe ^{3 +} ion content of the there is induced an increase in the surface potential under the same hydrogen peroxide concentration, this is because the action to Fe ³⁺ ion is an oxidizing agent, Fe ^{3 +} ions are the more increased the hydrogen peroxide to maintain the steel sheet surface potential Concentration tends to decrease.

Therefore, in a state where the metal concentration is sufficient, the surface potential of -0.2 V or more can be sufficiently secured by Fe ^{3 +} / Fe ^{2 +} and the redox potential. From this time, the surface potential of the steel sheet can be controlled from the redox potential of the solution. Can be.

Such a relationship is obtained by the inventors' unremitting experiments, and can be confirmed from the examples to be described below. By the above experiments, the present inventors can confirm that there is a relationship between the minimum hydrogen peroxide concentration according to the iron ion concentration in the solution and the redox potential of the solution to maintain the surface potential of the steel sheet above -0.2V. This is shown graphically in FIG. 3.

0 g / L ≤ [metal] <10 g / L, [H ₂ O ₂ ] _min = 4.5 g / L, ORP 600 mV

10 g / L ≤ [metal] <20 g / L, [H ₂ O ₂ ] _min = 2.5 g / L, ORP 500 mV

20 g / L ≤ [metal] <40 g / L, [H ₂ O ₂ ] _min = 0.5 g / L, ORP 400 mV

40 g / L ≤ [metal] <60 g / L, [H ₂ O ₂ ] _min = 0 to 0.2 g / L, ORP 350 mV

As can be seen from FIG. 3, when the iron ion concentration is 0, an effective hydrogen peroxide concentration of at least 4.5 g / l or more should be included, and when the iron ion concentration is 40 g / l or more, the solution may be at a hydrogen peroxide concentration of 0 to 0.2 g / l. The addition of additional hydrogen peroxide can be minimized because the redox potential (ORP) of the solution is maintained above -0.2 V, the pickling surface potential, by the iron ions in the solution. That is, as the metal content increases, the surface potential of the steel sheet is dependent on the redox potential of the solution rather than the content of hydrogen peroxide, so that operation can be performed at low cost even if the metal content in the solution is relatively high. This area therefore requires only a minimum of hydrogen peroxide to maintain the ORP of the solution above 350 mV.

That is, the hydrogen peroxide concentration satisfies the following equation (1) in relation to the iron ions in the mixed acid solution, and the redox potential (ORP) is represented by the following equation (2) or (3) in relation to the iron ion concentration in the mixed acid solution. It is desirable to satisfy).

Hydrogen peroxide concentration (g / l) ≥ 0.00736 + 10 × e- ^{[metal] /13.2} (1)

ORP ≥ 600 mV, provided that [metal] ≤ 10 g / l (2)

ORP (mV) ≥ 310 + 431 × e- ^{[metal] /25.24} , where [metal]> 10g / l (3)

In the formulas (1) to (3), [metal] represents the iron ion concentration in the mixed acid solution.

In the mixed acid pickling step, an excellent pickling effect can be obtained when the hydrogen peroxide concentration of the mixed acid solution in the mixed acid bath and the redox potential satisfy the above relation in the relationship with the iron ion concentration in the solution.

In performing such a mixed acid process, if the conditions of the mixed acid solution as described above are satisfied, even if the temperature of the mixed acid solution is not specifically controlled, the pickling effect to be obtained in the present invention can be obtained. Therefore, a person skilled in the art can perform the mixed acid pickling process by appropriately setting the solution temperature of the mixed acid bath. For example, a mixed acid pickling process may be performed by setting the temperature in a range of 20 to 95 ° C, as another example, 25 to 80 ° C, and as another example, 25 to 65 ° C.

From the above, it was confirmed that the concentration of sulfuric acid and hydrofluoric acid in the pickling solution and the concentration of residual hydrogen peroxide were the most important factors in increasing the pickling effect and high speed pickling in the mixed pickling process in the mixed acid bath. Therefore, it is necessary to control the concentration of these components, the concentration control of each of these components, it is possible to adjust the sulfuric acid and hydrofluoric acid concentration using a conventionally used acid analyzer, the residual hydrogen peroxide concentration through a near infrared analysis method or an automatic titration method Concentration can be analyzed and adjusted.

According to the method of the present invention as described above, the pickling process can be performed at a high speed, the total pickling time can be significantly shortened the time required for pickling of about 15 to 240 seconds, austenitic stainless steel having excellent quality Steel sheet can be obtained.

Example

Hereinafter, the present invention will be described in detail with reference to Examples. However, the following examples are intended to illustrate the present invention and are not intended to limit the present invention.

Example  One

In order to confirm the pickling properties of the oxide scale of the austenitic cold rolled steel sheet with or without neutral salt electrolysis and sulfuric acid electrolysis, an austenitic stainless steel sheet having a chromium composition of 16% by weight or more was subjected to neutral salt electrolytic treatment and sulfuric acid electrolytic treatment. The scale layer consisting of Cr, Mn, and Fe was removed, respectively.

At this time, the neutral salt electrolytic solution used includes sodium sulfate electrolyte 150g / l as an electrolyte, the temperature of the solution is 60 ℃, the current density of 20A / dm ² so that the potential on the surface of the steel sheet is formed in the order +,-, + Was applied for 40 seconds.

In addition, sulfuric acid electrolytic solution is a solution of pH 1 containing sulfuric acid 85g / l, the solution temperature is 50 ℃, applying a current of 20A / dm 2 for 15 seconds so that the potential of the steel plate surface is formed in the order +,-, + It was.

The surface of the steel plate subjected to the neutral salt electrolysis and the sulfuric acid electrolysis and the cross section of the untreated steel sheet were photographed with an electron microscope (SEM) and are shown in FIG. 1. For comparison, the cross section of the electrolytically treated steel sheet is shown in A), and the cross section of the steel sheet not subjected to the electrolytic treatment is shown in B).

As can be seen from FIG. 1, it can be seen that (Cr, Mn) ₃ O ₄ and silicon oxide remain at the same time on the cross-section of the steel sheet without neutral salt electrolysis and sulfuric acid electrolysis. It was confirmed that only silicon oxide remained in the cross section of the steel plate subjected to neutral salt electrolysis and sulfuric acid electrolysis.

Example  2

In order to observe the surface state of the cold rolled steel sheet according to the surface potential in the mixed acid tank, the silicon oxide film according to the surface potential was used by using a steel sheet whose primary scale was removed by the neutral salt electrolysis and the sulfuric acid electrolysis treatment obtained in Example 1 above. The pickling was evaluated.

The specimen was immersed in a mixed acid solution at 45 ° C. containing 120 g / l sulfuric acid and 20 g / l free hydrofluoric acid, followed by application of the potential for 30 seconds while changing the potential in the range of −0.4 to 0.6 V as shown in Table 1. Was performed.

After the pickling, the surface state of the cold rolled steel sheet was observed using a scanning electron microscope (SEM), and then the presence of pickling and the degree of grain boundary dissolution were evaluated.

If scale remains on the surface of the steel sheet, it is evaluated by fine pickling, and the degree of grain boundary dissolution is judged to be good when the grain boundary is continuously dissolved, and is represented by ○, and the case of discontinuity is not good, and is indicated by ×. It was. On the other hand, in the case of non-acid washing, the degree of grain boundary dissolution was not evaluated.

The evaluation results are shown in Table 1 below. Furthermore, the surface states of the steel sheets of Inventive Example 4 and Comparative Example 4 having applied potentials of 0.0 V and −0.25 V were photographed with an electron microscope (SEM) and shown in FIG. 2.

Applied potential (V) Pickling Intergranular melting Comparative Example 1 0.6 × - Comparative Example 2 0.4 × - Comparative Example 3 0.2 × - Inventory 1 0.1 ○ ○ Inventory 2 0.0 ○ ○ Inventory 3 -0.10 ○ ○ Honorable 4 -0.15 ○ ○ Inventory 5 -0.20 ○ ○ Comparative Example 4 -0.25 ○ × Comparative Example 5 -0.30 × - Comparative Example 6 -0.40 × -

As can be seen from Table 1, when the surface potential is -0.25 ~ 0.1V applied, pickling in a mixed acid solution was possible (Invention Examples 1 to 5 and Comparative Example 4). However, as can be seen from FIG. 2, in Comparative Example 4, the degree of grain boundary pickling was poor. That is, in the case of A) showing the steel plate surface obtained in Inventive Example 4, the grain boundary of the steel plate surface is normally dissolved, and the grain boundary is clearly shown, while in the case of B) showing the steel plate surface obtained in Comparative Example 4, the residual scale However, it was confirmed that the grain boundaries dissolve discontinuously, did not dissolve uniformly, and the grain boundaries were small.

On the other hand, in Comparative Examples 1, 2, 3, 5 and 6, the results of the acid pickling.

From these results, it was found that the surface potential in the mixed acid bath is applied in the range of -0.2 to 0.1V, which is suitable for dissolution and grain boundary dissolution of the Si oxide layer.

Example  3

The present Example is to confirm the relationship between the hydrogen peroxide concentration and the iron ion concentration to obtain a surface potential of -0.2V in mixed acid pickling of austenitic cold rolled steel sheet, the neutral salt electrolysis and sulfuric acid electrolytic treatment obtained in Example 1 Using the steel plate from which the primary scale was removed, the presence or absence of pickling of the silicon oxide film according to the surface potential was evaluated.

Was immersed in the mixed acid solution of 45 ℃ that the specimen comprises a sulfate 120g / l and a free hydrofluoric acid 20g / l, and with the addition of metal ions (Fe ^{3 +)} and hydrogen peroxide to the mixed acid solution, measuring the surface potential of the steel sheet, The minimum hydrogen peroxide concentration and the redox potential of the solution (ORP) were measured to maintain the surface potential of the steel sheet over -0.2V according to the iron ion concentration change, and the results are shown in FIG. 3.

3 is a graph illustrating the change in the minimum hydrogen peroxide concentration and the redox potential (ORP) of the solution according to the change in the concentration of iron ions in order to maintain the surface potential of the steel sheet -0.2V or more.

As can be seen from FIG. 3, as the iron ion concentration increases, the concentration of the minimum hydrogen peroxide for maintaining the surface potential of the steel sheet decreases gradually. As the metal concentration increases, the redox potential of the solution increases. It can be seen that (ORP) decreases, and when the metal concentration is 40g / l or more, even if the redox potential (ORP) of the solution is maintained at only 400mV, the surface potential of the strip is formed to be -0.2V, thus adding additional hydrogen peroxide solution. It is not necessary.

However, in the region where the redox potential (ORP) of the solution becomes less than 400 mV, the surface potential is changed, and it is necessary to input a minimum hydrogen peroxide to maintain the redox potential (ORP) of the solution at 400 mV.

Example  4

This example is intended to confirm the appropriate operating conditions when performing neutral salt electrolysis, except that the solution temperature, applied current, and sodium sulfate concentration of the neutral salt electrolyzer were adjusted and adjusted as shown in Table 2 below. Neutral salt electrolysis was carried out in the same manner as in Example 1.

The surface state of the steel plate after neutral salt electrolysis was observed, and the result is shown in Table 2 below.

When the surface state is bad, such as the presence of manganese chromium oxide scale on the surface of the steel plate after neutral salt electrolysis, it is represented by x, and when the steel plate surface state is good, it is represented by ○.

Temperature (℃) Current (A / dm²) Sodium sulfate concentration (g / l) Surface quality Comparative Example 1 30 20 250 × Comparative Example 2 50 5 250 × Comparative Example 3 50 10 50 × Inventory 1 50 10 100 ○ Inventory 2 90 30 250 ○

As can be seen from Table 2, the solution temperature in the electrolytic cell is 50 ~ 90 ℃, in the electrolytic solution containing sodium sulfate 100 ~ 250g / l, and neutral under the conditions having a current density of 10 ~ 30A / dm 2 When salt electrolysis was performed, the steel plate surface quality was excellent.

Example  5

This embodiment is intended to confirm the appropriate operating conditions in the case of sulfuric acid electrolysis, except that the solution temperature, applied current and sulfuric acid concentration of the sulfuric acid electrolyzer was adjusted to perform as described in Table 3 below, Neutral salt electrolysis was performed in the same manner as in Example 1.

The surface state of the steel plate after performing sulfuric acid electrolysis was observed, and the result is shown in Table 3 below.

The case where the surface state is poor, such as iron or manganese-chromium oxide scale remaining, is indicated by ×. The case where all iron or manganese-chromium oxide scales are removed and only the Si oxide scale remains is shown as ○. .

Temperature (℃) Current (A / dm ² ) Sulfuric acid concentration (g / l) Surface quality Comparative Example 1 30 5 50 × Comparative Example 2 70 5 150 × Comparative Example 3 70 30 150 × Comparative Example 4 30 10 30 × Inventory 1 30 10 50 ○ Inventory 2 60 20 150 ○

As can be seen from Table 3, the sulfuric acid electrolysis under the condition that the solution temperature in the sulfuric acid electrolytic cell is 30 ~ 60 ℃, sulfuric acid concentration in the electrolytic solution is 50 ~ 150g / l, the current density of 10 ~ 30A / dm ² In case of, the steel plate surface quality was excellent.

Example  6

This example is intended to confirm the proper treatment time of neutral salt electrolysis and sulfuric acid electrolysis, and neutral salt electrolysis as in Example 1 except that the neutral salt electrolysis and sulfuric acid electrolysis treatment times were adjusted as shown in Table 4. And sulfuric acid electrolytic treatment.

The surface state of the steel plate after neutral salt electrolysis and sulfuric acid electrolysis was observed, and the result is shown in Table 4 below.

The case where the scale of manganese, chromium or iron other than silicon oxide does not remain is indicated by (circle), and the case where the scale of manganese, chromium or iron other than silicon oxide remains is not acidic, and is judged to be superacid if there is erosion of the base metal. In addition, when a non-acid tax and an over-acid tax appear, it represented with x.

Neutral Salt Treatment Time (s) Sulfuric Acid Electrolytic Treatment Time (s) Pickling Comparative Example 1 0 30 × Comparative Example 2 0 60 × Comparative Example 3 0 90 × Comparative Example 4 90 70 X (perpetual tax) Comparative Example 5 120 0 × Comparative Example 6 130 0 × Comparative Example 7 130 60 X (perpetual tax) Inventory 1 30 50 ○ Inventory 2 90 5 ○ Inventory 3 50 50 ○ Honorable 4 90 30 ○ Inventory 5 120 50 ○

As can be seen from Table 4, when the neutral salt electrolysis is performed in the range of 30 to 120 seconds and the sulfuric acid electrolysis is performed in the range of 5 to 50 seconds, the stainless steel cold rolled steel sheet as shown in Fig. 1A) Although only Si oxide was present on the surface, Comparative Examples 1 to 4, which deviated from the above ranges, had a surface state as shown in B) of FIG. 1, such that a scale of (Cr · Mn) ₃ O ₄ existed or the surface was damaged. Could confirm.

Example  7

This embodiment is intended to confirm the appropriate treatment conditions in the mixed acid tank, the mixed acid solution of the composition shown in Table 5 for the steel sheet from which the primary scale is removed by the neutral salt electrolysis and sulfuric acid electrolytic treatment obtained in Example 1 and Mixed acid pickling was performed as treatment conditions. At this time, the treatment temperature of the mixed acid solution was 40 ~ 45 ℃, the hydrogen peroxide concentration was adjusted to the hydrogen peroxide concentration in order to maintain the surface potential of the steel sheet at -0.1V according to the iron concentration in the solution from Example 3 and FIG.

The presence or absence of pickling of the silicon oxide film on the surface of the steel sheet obtained by the mixed acid treatment was observed, and the results are shown in Table 5 below.

The case where silicon oxide does not remain is indicated by ○, and the case where silicon oxide remains is not pickled, even if pickled, if the glossiness measured at a reflection angle of 60 ° in the rolling direction is less than 150, it is judged to be superacid Indicated.

Sulfuric acid (g / l) Foshan (g / l) Time (s) Pickling Result Comparative Example 1 60 10 30 X (non-tax) Comparative Example 2 60 15 100 X (non-tax) Comparative Example 3 60 20 30 X (non-tax) Comparative Example 4 60 20 100 X (non-tax) Comparative Example 5 60 25 30 X (non-tax) Comparative Example 6 110 10 10 X (non-tax) Inventory 1 110 15 10 ○ Inventory 2 110 15 30 ○ Inventory 3 110 20 10 ○ Honorable 4 110 20 30 ○ Inventory 5 110 25 10 ○ Inventory 6 110 25 100 ○ Honorable 7 110 30 30 ○ Comparative Example 7 110 40 100 X (perpetual tax) Comparative Example 8 150 10 10 X (non-tax) Honors 8 150 15 30 ○ Proposition 9 150 25 30 ○ Comparative Example 10 200 20 100 X (perpetual tax)

As can be seen from Table 5, sulfuric acid 110 ~ 150g / l, free hydrofluoric acid 15 ~ 25g / l and the minimum hydrogen peroxide according to the iron ion concentration is deposited in a pickling composition made in Example 3 for 10 to 100 seconds mixed acid It is understood that pickling is preferable.

Claims (11)

As a pickling method of a high chromium austenitic stainless steel cold rolled steel sheet which removes silicon oxide from a high chromium austenitic stainless steel cold rolled steel sheet containing 16% by weight or more of chromium,
Silicon oxide is removed from the cold rolled steel sheet by immersing the cold rolled steel sheet in a mixed acid solution containing no nitric acid and containing 110-150 g / l sulfuric acid, 15-25 g / l free hydrofluoric acid, and hydrogen peroxide,
The hydrogen peroxide concentration in the mixed acid solution satisfies the following equation (1) in relation to the iron ion concentration in the mixed acid solution, and the redox potential (ORP) is represented by the following equation (2) in relation to the iron ion concentration in the mixed acid solution or Pickling method of high chromium austenitic stainless steel cold rolled steel sheet which satisfies (3).
Hydrogen peroxide concentration (g / l) ≥ 0.00736 + 10 × e- ^{[metal] /13.2} (1)
ORP ≥ 600 mV, provided that [metal] ≤ 10 g / l (2)
ORP (mV) ≥ = 310 + 431 × e- ^{[metal] /25.24} , where [metal]> 10g / l (3)
In the formulas (1) to (3), [metal] represents the iron ion concentration in the mixed acid solution.
The method of claim 1, wherein the mixed acid solution is a high chromium austenitic stainless steel cold rolled steel sheet having an iron ion concentration of 0 g / l at the beginning of the pickling process.
The method of claim 1, wherein the surface potential of the cold rolled steel sheet immersed in the mixed acid solution is maintained at -0.2 to 0.1V.
The method of claim 1, wherein the cold rolled steel sheet is immersed in the mixed acid solution for 10 to 100 seconds.
The method of claim 1, wherein the removal of silicon oxide from the cold rolled steel sheet is carried out after the neutral salt electrolytic treatment step and sulfuric acid electrolytic treatment step, or sulfuric acid electrolytic treatment step,
The neutral salt electrolytic treatment step of electrolytic removal of the Cr-rich scale from the surface of the steel sheet using an electrolytic solution containing sodium sulfate electrolyte,
The sulfuric acid electrolytic treatment step is a pickling method of a high chromium austenitic stainless steel cold rolled steel sheet to electrolytically remove the residual scale of Cr and Fe using an electrolyte solution containing sulfuric acid as an electrolyte.
The method of claim 5, wherein the neutral salt electrolysis step is to immerse the austenitic stainless steel sheet in a neutral salt electrolytic solution at a temperature of 50 ~ 90 ℃, 10 ~ 30A so that the potential of the surface of the steel sheet is formed in the order of +,-, + A pickling method for a high chromium austenitic stainless steel cold rolled steel sheet by applying a current density of / dm ² for 30 to 120 seconds.
The method for pickling a high chromium austenitic stainless steel cold rolled steel sheet according to claim 6, wherein the neutral salt electrolytic solution contains 100-250 g / l sodium sulfate electrolyte.
6. The method of claim 5, wherein the sulfuric acid electrolysis step is immersed in an austenitic stainless steel sheet subjected to a neutral salt electrolysis step in a sulfuric acid electrolytic solution at a temperature of 30 ~ 60 ℃, so that the potential of the surface of the steel sheet is formed in the order +,-, + A method of pickling high chromium austenitic stainless steel cold rolled steel sheet by applying a current density of 10 to 30 A / dm ² for 5 to 50 seconds.
9. The method of claim 8, wherein the sulfuric acid electrolytic solution contains 50-150 g / l sulfuric acid.
delete A mixed acid solution for removing silicon oxide from a high chromium austenitic stainless steel cold rolled sheet containing 16 wt% or more of chromium,
It contains no nitric acid, sulfuric acid 110-150g / l, free hydrofluoric acid 15-25g / l and hydrogen peroxide, the hydrogen peroxide concentration satisfies the following formula (1) in relation to the iron ions in the mixed acid solution, The redox potential (ORP) is a mixed acid solution that satisfies the following formula (2) or (3) in relation to the iron ion concentration in the mixed acid solution.
Hydrogen peroxide concentration (g / l) ≥ 0.00736 + 10 × e- ^{[metal] /13.2} (1)
ORP ≥ 600 mV, provided that [metal] ≤ 10 g / l (2)
ORP (mV) ≥ 310 + 431 × e- ^{[metal] /25.24} , where [metal]> 10g / l (3)
In the formulas (1) to (3), [metal] represents the iron ion concentration in the mixed acid solution.

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