JP2017218643A - Manufacturing method of electroplated steel sheet - Google Patents

Abstract

PROBLEM TO BE SOLVED: To make plate thickness which is finally obtained uniform and provide beautiful surface appearance by making the coating mass of a plating liquid remaining on a steel sheet between electroplated cells uniform.SOLUTION: There is provided a manufacturing method of an electroplated steel sheet by conducting electroplating on a steel sheet 1 with a plurality of cells continuously, a spray nozzle 8 is arranged in a steel sheet width direction at a steel sheet 1 outlet side of the electroplating cell, a solution with pH of 4 to 7 is injected toward the steel sheet from the spray nozzle 8, further a slit gas nozzle 9 having a longer injection port than width of the steel sheet is arranged in the steel sheet width direction in a downstream side of the spray nozzle and gas is injected toward the steel sheet from the slit gas nozzle 9.SELECTED DRAWING: Figure 1

Description

  The present invention relates to a method for producing an electroplated steel sheet, and relates to a method for producing an electroplated steel sheet having a uniform plating thickness and a beautiful surface appearance.

  In the production of electroplated steel sheets, horizontal and vertical flow cell systems and radial cell systems are known as general electroplating systems for steel sheets.

  As shown in FIG. 4, the horizontal flow cell type cell structure has a structure in which current-carrying rolls 2 are installed on the entrance side and exit side of the strip (steel plate) 1, and anode electrodes 3 are installed on the front and back surfaces of the strip 1. is there. The strip 1 is run in the horizontal direction (in the direction of the arrow), the plating solution 4 is supplied to the gap between the strip 1 and the anode electrode 3, and current is passed between the front and back surfaces of the strip 1 that is the cathode and the anode electrode 3. It is plated by doing.

  As shown in FIG. 5, the vertical flow cell type cell structure has the strip 1 run in the horizontal direction (in the direction of the arrow) and the running direction is changed downward by the energizing roll 2 installed on the entrance side of the strip 1. The traveling direction of the strip 1 is changed upward by the sink roll 6, and the traveling direction of the strip 1 is changed to the horizontal direction by the energizing roll 2 installed on the outlet side of the strip 1. An anode electrode 3 is installed on the front and back surfaces of the strip 1 between the energizing roll 2 and the sink roll 6, and a plating solution 4 is supplied to the gap between the strip 1 and the anode electrode 3 by the flow nozzle 5 to serve as a cathode. Plating is performed by energizing between the front and back surfaces of the strip 1 and the anode electrode 3.

  As shown in FIG. 6, the radial cell type cell structure has the strip 1 run in the horizontal direction (in the direction of the arrow), and the running direction is changed downward by the through plate roll 7 installed on the entrance side of the strip 1. In this structure, the running direction of the strip 1 is changed upward by the energizing roll 2, and the running direction of the strip 1 is changed to the horizontal direction by the through plate roll 7 installed on the exit side of the strip 1. The strip 1 is wound around the energizing roll 2 and immersed in the plating solution 4, and the plating solution 4 is supplied by the flow nozzle 5 to the gap between the strip 1 and the arcuate anode electrode 3 placed on the circumference facing the strip 1. Then, plating is carried out by energizing between the plating surface of the strip 1 as the cathode and the anode electrode 3.

  The flow cell method has an advantage that the front and back surfaces of the steel plate can be plated simultaneously. The radial cell method is a single-sided plating method. However, in the radial cell method, the distance between the plating surface of the strip and the anode electrode can be reduced by running the strip around the energizing roll. For this reason, the resistance in electroplating is reduced, and there is an advantage that a high current density can be obtained at a low voltage.

In the case of electrogalvanization which is typical in electroplating, usually 5 to 15 cells are arranged in series, and the plating process is continuously performed while passing the steel plate. The plating adhesion amount per cell is as thin as 1 to 5 g / m ^2, and this is a plating method in which these are laminated, and the current can be controlled according to the line speed and plate width, so the adhesion amount in the width direction and longitudinal direction It is also a great feature that the distribution can be made uniform within 0.5-1 g / m ² and a beautiful appearance can be obtained. On the other hand, as compared with continuous hot dip galvanization in which annealing and galvanization are performed on the same line, the price of an electroplated steel sheet in which annealing and galvanization are processed on separate lines is likely to be high.

Therefore, in recent years, in order to improve the productivity of the electroplating line, various studies have been made to increase the plating current density and achieve improvement in uniformity. Usually, using a plating solution having a pH of about 1.5 to 2.0, the current density is about 100 A / dm ^{2 at the} maximum.

  In Patent Document 1, the plating solution is jetted in the direction opposite to the steel plate traveling direction so that the flow of the plating solution between the anode and the steel plate is uniform in the width direction, and the plating solution is jetted onto the steel plate surface at the electrode entrance / exit side. A method is disclosed in which plating is performed by spraying a plating solution toward a steel sheet while sealing the plating solution flowing out.

  Patent Document 2 discloses an electroplating method that enables uniform plating by dividing the inside of a cushion-shaped nozzle in the width direction to provide a plating solution flow rate distribution.

  Patent Document 3 discloses a method of making the flow rate of the plating solution uniform by gradually increasing the nozzle slit opening for supplying the plating solution from the center of the plate width toward the end of the plate width.

  Patent Document 4 discloses a method of lowering the pH of the plating solution and setting the plating solution temperature and the liquid flow rate to predetermined conditions in order to increase the current density.

JP 59-85891 A JP 59-96293 A Japanese Patent Laid-Open No. 61-099695 Japanese Patent Laid-Open No. 06-136594

  However, in the methods described in Patent Documents 1 to 3, even if the plating adhesion amount in the plating cell can be made uniform, the adhesion amount of the plating solution remaining on the steel sheet surface is non-uniform in the non-plating range between the cells. Then, the plating film is dissolved by the remaining plating solution, and the plating thickness becomes non-uniform. As a result, the finally obtained plating thickness also becomes non-uniform. At the same time, the crystal orientation of the plating film becomes non-uniform, which causes uneven appearance (unevenness of whiteness).

  Further, as in Patent Document 4, when the pH of the plating solution is lowered in order to increase the current density, the amount of plating film dissolved by the remaining plating solution increases in the non-plating range between cells, and finally obtained. The uneven plating thickness and the uneven appearance are more pronounced.

  In view of the above circumstances, the present invention makes uniform the plating thickness remaining on the steel plate between the electroplating cells, thereby obtaining a uniform plating thickness and a beautiful surface appearance. For the purpose.

The gist of the present invention is as follows.
[1] A method for producing an electroplated steel sheet by continuously performing electroplating on a steel sheet, wherein a spray nozzle is provided in the width direction of the steel sheet on the steel sheet exit side of the electroplating cell, and a pH 4-7 solution from the spray nozzle. In addition, a slit gas nozzle having an injection port longer than the width of the steel plate is provided in the steel plate width direction on the downstream side of the spray nozzle, and gas is injected from the slit gas nozzle toward the steel plate. A method for producing an electroplated steel sheet.
[2] The electroplating steel sheet according to [1], wherein the electroplating cell is a horizontal flow cell, and slit gas nozzles are provided on the front and back surfaces of the steel sheet downstream from the energizing roll installed on the outlet side of the steel sheet. Production method.
[3] The method for producing an electroplated steel sheet according to [1], wherein the electroplating cell is a radial cell, and a spray nozzle and a slit gas nozzle are provided on the front and back surfaces of the steel sheet on the downstream side of the energizing roll.
[4] The slit gas nozzle has a nozzle slit gap of 0.3 to 2.0 mm, a distance between the nozzle tip and the steel plate of 5 to 100 mm, and an injection pressure of 1 to 10 kPa. [1] to [3 ] The manufacturing method of the electroplating steel plate in any one of.
[5] The method for producing an electroplated steel sheet according to any one of [1] to [4], wherein the plating solution has a pH of -0.5 to 1.0.
[6] The method for producing an electroplated steel sheet according to any one of [1] to [5], wherein the current density is 150 to 1200 A / dm ² .
[7] An apparatus for producing an electroplated steel sheet that performs electroplating on a steel sheet that continuously travels in the electroplating cell, and sprays a solution of pH 4 to 7 toward the steel sheet exit side of the electroplating cell. An apparatus for producing an electroplated steel plate, comprising: a spray nozzle in the steel plate width direction; and further comprising a slit gas nozzle in the steel plate width direction on the downstream side of the spray nozzle having an injection port having a width longer than the width of the steel plate.

  According to the present invention, the amount of the plating solution remaining on the steel plate between the electroplating cells can be controlled uniformly, so that the final plating thickness can be made uniform and a beautiful surface appearance can be obtained. It becomes possible. Further, according to the present invention, even if plating is performed at a high current density using a low pH plating solution, it is possible to make the finally obtained plating thickness uniform and obtain a beautiful surface appearance.

FIG. 1 is a diagram showing a horizontal flow cell type electroplating cell structure according to an embodiment of the present invention. FIG. 2 is a view showing a cell structure of a vertical flow cell type electroplating according to an embodiment of the present invention. FIG. 3 is a diagram showing a cell structure of radial cell electroplating according to the embodiment of the present invention. FIG. 4 is a diagram showing a cell structure of a conventional horizontal flow cell type electroplating. FIG. 5 is a view showing a cell structure of a conventional vertical flow cell type electroplating. FIG. 6 is a diagram showing a cell structure of a conventional radial cell type electroplating.

  Hereinafter, the electroplating method of the present invention will be described with reference to FIGS. In the present embodiment, one surface of the strip 1 is referred to as a front surface and the other surface is referred to as a back surface for convenience.

  FIG. 1 is a diagram showing a horizontal flow cell type electroplating cell structure according to an embodiment of the present invention. The strip 1 is run in the horizontal direction, the plating solution 4 is supplied to the gap between the strip 1 and the anode electrode 3, and the electroplating is performed by energizing between the plating surface of the strip 1 as the cathode and the anode electrode 3.

  On the exit side of the strip 1, a plurality of spray nozzles 8 for spraying a solution of pH 4 to 7 toward the strip 1 are provided in the width direction. On the further downstream side of the spray nozzle 8, a slit gas nozzle 9 having an injection port having a width longer than the width of the strip 1 is installed in the steel plate width direction toward the strip 1, and gas is injected toward the strip 1.

  Most of the plating solution 4 is dammed up by the energizing roll 2 installed on the exit side of the strip 1. However, when the shape of the steel plate is bad (for example, an ear wave shape) or due to wear of the energizing roll 2, the plating solution 4 may slip through the energizing roll 2 on the strip 1 exit side. As a result of intensive studies by the present inventors, in the non-plating range between the electroplating cells, if the amount of the acidic plating solution remaining on the steel sheet surface is uneven, the plating film is dissolved by the remaining plating solution. The plating thickness becomes non-uniform. As a result, it was found that the finally obtained plating thickness was non-uniform. At the same time, it was found that the crystal orientation of the plating film also became non-uniform, causing uneven appearance (unevenness of whiteness).

  Therefore, in the present invention, the spray nozzle 8 is installed on the outlet side of the strip 1, and the solution of pH 4 to 7 is sprayed from the spray nozzle 8 toward the strip 1, whereby the acidity of the strongly acidic plating solution remaining in the strip 1 is increased. The plating surface of the strip 1 is kept in a weakly acidic state. Thereby, dissolution of the plating film by the plating solution is suppressed. Further, by installing a slit gas nozzle 9 having an injection port longer than the width of the steel plate on the downstream side of the spray nozzle 8 and injecting a gas from the slit gas nozzle 9 toward the strip 1, a solution having a pH of 4 to 7 is injected. After that, the remaining liquid adhering to the surface of the strip 1 (hereinafter also referred to simply as “remaining liquid”. The remaining liquid is a solution having a pH of 4 to 7 sprayed by the spray nozzle 8 and has an acidity level. This is a solution containing both weakened plating solutions.) Since the liquid remaining on the steel plate remains acidic, the plating will dissolve if left untreated. Therefore, gas is injected from the slit gas nozzle 9 to prevent the dissolution amount of the plating film from being biased. As a result, the liquid film of the plating solution remaining on the steel sheet surface can be made uniform in the non-plating range between the electroplating cells. Therefore, the finally obtained plating thickness can be made uniform, and a beautiful surface appearance can be obtained.

  The solution sprayed to the strip 1 needs to have a function of preventing the dissolution of the plating film by weakening the acidity of the acidic plating solution remaining in the strip 1. Therefore, the pH of the solution sprayed onto the strip 1 is 4-7. When the pH is less than 4, the effect of weakening the acidity of the acidic plating solution is small. On the other hand, when the pH exceeds 7, the metal ions in the plating solution are hydrated and a hydroxide is generated on the surface of the strip 1, and there is a high possibility of causing scratches and the like.

  The amount of the solution sprayed onto the strip 1 needs to be set so that the pH of the solution after spray attached to the strip 1 exceeds 1. Although it is desirable that the pH of the solution after spraying attached to the strip 1 is higher, it is necessary to make the pH lower than the pH at which the metal ions in the plating solution are hydrated and the hydroxide is generated on the surface of the strip 1. Further, it is necessary to determine the amount of the solution to be ejected in consideration of the amount of the remaining liquid reduced by the slit gas nozzle 9 and the scattered state of the remaining liquid.

  Since the sprayed pH 4-7 solution remaining on the surface of the strip 1 is small, when the strip 1 is electroplated in the downstream plating cell among the connected plating cells, the plating solution composition and pH are reduced. The effect on the power is almost negligible.

  The spray nozzles 8 may be provided in the width direction of the strip 1 because a solution having a pH of 4 to 7 may be sprayed over the entire width of the strip 1. Further, the spray nozzle 8 and the slit gas nozzle 9 are desirably installed on the downstream side of the energizing roll 2 installed on the outlet side of the strip 1 in order to prevent the solution of pH 4 to 7 from being mixed into the cell. The spray nozzles 8 are preferably installed on the front and back surfaces of the strip 1, respectively, and are desirably offset by 100 mm or more in the longitudinal direction of the strip 1.

  The slit gas nozzle 9 has an injection port having a width longer than the width of the strip 1. This is because it is necessary to make the liquid film of the remaining liquid of the entire width of the strip uniform.

  Further, it is desirable that the slit gas nozzles 9 are respectively installed on the front and back surfaces of the strip 1. When the slit gas nozzle 9 installed on the front surface side of the strip 1 is at a position facing the slit gas nozzle 9 installed on the back surface side of the strip 1, the gas injected from the upper and lower slit gas nozzles 9 on the outer side in the width direction of the strip 1. Due to the collision, the plating solution 4 is likely to be scattered over a wide range. For this reason, when the slit gas nozzles 9 are installed on the front and back surfaces of the strip 1, the slit gas nozzle 9 installed on the front surface side of the strip 1 and the slit gas nozzle 9 installed on the back surface side are offset by 100 mm or more in the longitudinal direction of the strip 1 ( It is desirable to shift the position).

  FIG. 2 is a view showing a cell structure of a vertical flow cell type electroplating according to an embodiment of the present invention. The traveling direction of the strip 1 is changed downward by the energizing roll 2, and the plating solution 4 is supplied to the gap between the strip 1 and the anode electrode 3 through the flow nozzle 5, and the plating surface and the anode of the strip 1 that is the cathode Electroplating is performed by energizing between the electrodes 3.

  A spray nozzle 8 is installed on the exit side of the strip 1 in the width direction of the steel plate, and a solution having a pH of 4 to 7 is sprayed from the spray nozzle 8 toward the strip 1. Further, a slit gas nozzle 9 having an injection port longer than the width of the steel plate is installed on the downstream side of the spray nozzle 8 to inject gas toward the strip 1. The spray nozzle 8 weakens the acidity of the strong acidic plating solution remaining on the strip 1, keeps the plating surface of the strip 1 in a weakly acidic state, and suppresses dissolution of the plating film by the plating solution 4. Further, by jetting gas from the slit gas nozzle 9 toward the strip 1, the film thickness of the remaining liquid adhering to the surface of the strip 1 is made uniform. As a result, the liquid film of the plating solution remaining on the steel sheet surface can be made uniform in the non-plating range between the electroplating cells. Therefore, the finally obtained plating thickness can be made uniform, and a beautiful surface appearance can be obtained.

  The spray nozzles 8 may be provided in the width direction of the strip 1 because a solution having a pH of 4 to 7 may be sprayed over the entire width of the strip 1. Further, the spray nozzle 8 and the slit gas nozzle 9 are desirably installed on the downstream side of the energizing roll 2 installed on the outlet side of the strip 1 in order to prevent the solution of pH 4 to 7 from being mixed into the cell. The spray nozzles 8 are preferably installed on the front and back surfaces of the strip 1, respectively, and are desirably offset by 100 mm or more in the longitudinal direction of the strip 1.

  The pH of the solution sprayed onto the strip 1 is 4 to 7 as in the case of the horizontal flow cell method described above, and the amount of solution is such that the pH of the liquid adhering to the strip 1 after spraying exceeds 1. Set.

  Further, a solution having a pH of 4 to 7 is present before (upstream) the spray nozzle 8 installed on the surface side of the strip 1 on the exit side of the strip 1 (upper surface of the steel plate when the strip 1 is run in the horizontal direction). In order to prevent mixing in the cell, a roll 10 may be separately installed.

  Further, it is desirable that the slit gas nozzles 9 are respectively installed on the front and back surfaces of the strip 1. The slit gas nozzles 9 installed on the front and back surfaces of the steel sheet are preferably offset by 100 mm or more in the longitudinal direction of the strip 1 in order to prevent the plating solution from scattering due to collision of gas injected from the upper and lower slit gas nozzles 9.

  FIG. 3 is a diagram showing a cell structure of radial cell electroplating according to the embodiment of the present invention. The strip 1 is wound around the energizing roll 2 to travel, and the plating solution 4 is supplied to the gap between the strip 1 and the anode electrode 3 through the flow nozzle 5, and the plating surface of the strip 1 as the cathode and the anode electrode 3 are supplied. And electroplating.

  A spray nozzle 8 is installed on the exit side of the strip 1 in the width direction of the steel plate, and a solution having a pH of 4 to 7 is sprayed from the spray nozzle 8 toward the strip 1. Further, a slit gas nozzle 9 having an injection port longer than the width of the steel plate is installed on the downstream side of the spray nozzle 8 to inject gas toward the strip 1. The spray nozzle 8 weakens the acidity of the strong acidic plating solution remaining on the strip 1, keeps the plating surface of the strip 1 in a weakly acidic state, and suppresses dissolution of the plating film by the plating solution 4. Further, by jetting gas from the slit gas nozzle 9 toward the strip 1, the film thickness of the remaining liquid adhering to the surface of the strip 1 is made uniform. As a result, the liquid film of the plating solution remaining on the steel sheet surface can be made uniform in the non-plating range between the electroplating cells. Therefore, the finally obtained plating thickness can be made uniform, and a beautiful surface appearance can be obtained.

  The spray nozzles 8 may be provided in the width direction of the strip 1 because a solution having a pH of 4 to 7 may be sprayed over the entire width of the strip 1. In addition, the spray nozzle 8 and the slit gas nozzle 9 are desirably installed on the downstream side of the sheet passing roll 7 installed on the exit side of the strip 1 in order to prevent the solution of pH 4 to 7 from entering the cell. The spray nozzles 8 are preferably installed on the front and back surfaces of the strip 1, respectively, and are desirably offset by 100 mm or more in the longitudinal direction of the strip 1.

  The pH of the solution sprayed onto the strip 1 is 4 to 7 as in the case of the horizontal flow cell method described above, and the amount of solution is such that the pH of the liquid adhering to the strip 1 after spraying exceeds 1. Set.

  Further, a solution having a pH of 4 to 7 is present before (upstream) the spray nozzle 8 installed on the surface side of the strip 1 on the exit side of the strip 1 (upper surface of the steel plate when the strip 1 is run in the horizontal direction). In order to prevent mixing in the cell, a roll 10 may be separately installed.

  Further, it is desirable that the slit gas nozzles 9 are respectively installed on the front and back surfaces of the strip 1. The slit gas nozzles 9 installed on the front and back surfaces of the steel sheet are preferably offset by 100 mm or more in the longitudinal direction of the strip 1 in order to prevent the plating solution from scattering due to collision of gas injected from the upper and lower slit gas nozzles 9.

  In the present invention, the form of the spray nozzle 8 is not particularly limited. For example, the liquid is ejected over the entire width direction of the strip 1 using a full cone type nozzle that ejects droplets in a conical shape from the ejection port. Thus, a plurality of spray nozzles 8 may be arranged in the width direction.

  The type of the pH 4-7 solution is preferably matched to the type of the plating solution 4. For example, in the case of a sulfuric acid-based plating solution, sulfuric acid adjusted to pH 4 to 7 may be used.

  As the gas of the slit gas nozzle 9, air is preferable from the viewpoint of cost and environmental measures. An inert gas such as nitrogen gas can also be used.

  The nozzle gap of the slit gas nozzle 9 is desirably 0.3 to 2.0 mm. If it is less than 0.3 mm, the effect of reducing the amount of the plating solution cannot be obtained sufficiently, and nozzle clogging due to the scattered plating solution tends to occur. On the other hand, if the nozzle gap exceeds 2.0 mm, surplus gas is injected, and the plating solution is likely to be scattered, which in turn deteriorates the surface appearance. The nozzle gap is more preferably 0.3 to 1.5 mm.

  In the present invention, the distance between the slit gas nozzle 9 and the strip 1 is preferably 5 to 100 mm. If the distance is less than 5 mm, the slit gas nozzle 9 and the strip 1 may come into contact with each other. If the distance between the slit gas nozzle 9 and the strip 1 exceeds 100 mm, the effect of reducing the amount of plating solution cannot be obtained sufficiently. The distance between the slit gas nozzle 9 and the strip 1 is more preferably 5 to 50 mm.

  The injection pressure of the slit gas nozzle 9 is desirably 1 to 10 kPa. If it is lower than 1 kPa, the effect of reducing the amount of plating solution cannot be obtained sufficiently. On the other hand, if it exceeds 10 kPa, the plating solution is likely to scatter, which in turn deteriorates the surface appearance. It is more desirable to change the injection pressure of the slit gas nozzle 9 according to the line speed (low pressure at low speed and high pressure at high speed).

  The present invention is effective in plating uniformity and appearance unevenness even with a normal plating solution (pH = 1.5 to 2.0). However, when the pH of the plating solution is -0.5 to 1.0 in order to increase the current density, the effect of the present invention appears more clearly.

In the present invention, it is preferred that the current density is 150~1200A / dm ^2. When the current density is less than 150 A / dm ² , the sheet passing speed cannot be sufficiently increased, and the time for passing through the non-plating region between the plating cells becomes long, and the appearance defect and the adhesion amount distribution are liable to be deteriorated. . On the other hand, when the current density exceeds 1200 A / dm ² , “plating burn” occurs in which the plating surface becomes black due to the change in the orientation of the plating film crystal.

In the case of the flow cell method, since the current flows in the longitudinal direction inside the steel plate (from the anode electrode toward the energizing roll), the current density can be increased up to 400 A / dm ^{2 in} terms of the limit of heat generation of the steel plate. become. Further, in the case of the radial cell method, since the current flows in the thickness direction inside the steel sheet, the temperature of the steel sheet hardly increases and the current density can be increased up to 1200 A / dm ^{2 at the} maximum.

  Examples of the present invention will be described below. The technical scope of the present invention is not limited to the following examples.

The example which used the electroplating cell provided with the structure shown in FIGS. 1-3 was electroplated as an example of this invention, and the electroplated steel plate was manufactured. As the strip 1, a cold-rolled steel strip having a thickness of 0.5 mm and a width of 1000 mm was run at a line speed of 2.07 to 5.0 m / s. The anode electrode 3 is titanium, the energized surface is coated with an iridium oxide film, and has a width that substantially covers the strip 1. As the plating solution 4, solutions having different pHs and a zinc sulfate concentration of 400 g / L were used at 60 ° C. The plating adhesion amount was set such that the lower limit of one side was 20 g / m ² . As the liquid sprayed from the spray nozzle 8, sulfuric acid having an appropriately adjusted pH was used.

The plating thickness calculated the average value which measured 3 points | pieces in the width direction 10 times in the longitudinal direction, and calculated distribution (maximum-minimum) of the plating adhesion amount. When the distribution of plating adhesion was within 2.0 g / m ² , the plating thickness was assumed to be uniform.

  The surface appearance is evaluated using the L value at the same location as the adhesion amount measurement using a colorimeter, and 5 (good) when the whiteness is high and the variation is small, and 1 (poor) when the whiteness is low and the variation is large. As a result, it was evaluated in five stages. Of the five stages, 4 or more were accepted.

  The plating conditions and results are shown in Table 1.

  From the results of Table 1, when electroplating is performed using the cell of the present invention, the plating thickness is uniform and the surface appearance is beautiful.

1 Strip (steel plate)
2 Energizing roll 3 Anode electrode 4 Plating solution 5 Flow nozzle 6 Sink roll 7 Passing plate roll 8 Spray nozzle 9 Slit gas nozzle 10 Roll

Claims (7)

  A method for producing an electroplated steel sheet by continuously electroplating a steel sheet, wherein a spray nozzle is provided in the width direction of the steel sheet on the steel sheet exit side of the electroplating cell, and a solution having a pH of 4 to 7 is applied to the steel sheet from the spray nozzle. In addition, a slit gas nozzle having an injection port longer than the width of the steel plate is provided in the steel plate width direction on the downstream side of the spray nozzle, and gas is injected from the slit gas nozzle toward the steel plate. A method of manufacturing a steel sheet.   The electroplating cell is either a horizontal flow cell or a vertical flow cell, and is characterized in that a spray nozzle and a slit gas nozzle are provided on the front and back surfaces of the steel sheet on the downstream side of the energizing roll installed on the outlet side of the steel sheet. Item 2. A method for producing an electroplated steel sheet according to Item 1.   The method for producing an electroplated steel sheet according to claim 1, wherein the electroplating cell is a radial cell, and a spray nozzle and a slit gas nozzle are provided on the front and back surfaces of the steel sheet on the downstream side of the energizing roll.   The slit gas nozzle has a nozzle slit gap of 0.3 to 2.0 mm, a distance between the nozzle tip and the steel plate of 5 to 100 mm, and an injection pressure of 1 to 10 kPa. The manufacturing method of the electroplated steel plate of description.   The method for producing an electroplated steel sheet according to any one of claims 1 to 4, wherein the plating solution has a pH of -0.5 to 1.0. Method of manufacturing an electro-plated steel sheet according to any one of claims 1 to 5, wherein the current density is 150~1200A / dm ^2. An apparatus for producing an electroplated steel sheet that performs electroplating on a steel sheet continuously running in an electroplating cell,
On the steel sheet exit side of the electroplating cell, a spray nozzle for injecting a solution of pH 4 to 7 toward the steel sheet is provided in the steel sheet width direction,
Furthermore, the manufacturing apparatus of the electroplated steel plate characterized by providing the slit gas nozzle which has a jet nozzle longer than the width of a steel plate in the steel plate width direction downstream of a spray nozzle.

Images