JP2014019906A - Production device for electroplated steel sheet - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a production device for an electroplated steel sheet in which the repair of a worn insoluble electrode is facilitated, further, only the worn part can be repaired, and repair cost can be reduced.SOLUTION: The production device comprises: an insoluble electrode of performing energizing to a space with a steel sheet and continuously performing electroplating to the running steel sheet; and a plurality of engagement members sagged with a self fluxing electrode and the insoluble electrode, respectively, and electrically connected with the self fluxing electrode and the insoluble electrode. The insoluble electrode has: a body part in which the maximum face is confronted with the steel sheet; and a contact part engaged by each engagement member and further electrically connected, and the body part and the contact part are detachably formed.

Description

  The present invention relates to an apparatus for producing an electroplated steel sheet that uses a self-fluxing electrode and an insoluble electrode to perform electroplating while consuming the self-fluxing electrode.

Conventionally, manufacture of an electroplated steel sheet such as tin plating is performed by applying electricity to the steel sheet and the electrode. Examples of the electroplated steel sheet include tin plating and zinc plating. For example, tin plating is performed on an electro tinning line (ETL) for electroplating tin (see Patent Document 1). .
In such an electric tin plating line, that is, a tin-plated steel sheet production line, when an insoluble electrode is used, tin ions are supplied by a chemical. On the other hand, when a soluble or self-fluxing tin electrode is used as the anode, tin ions are supplied by melting the tin electrode itself. Therefore, the tin electrode itself is consumed over time. Therefore, when a self-fluxing tin electrode is used in a continuous plating line, the electrode is replaced or replenished every time a predetermined amount is consumed.

Thus, when electroplating using a self-fluxing tin electrode, the tin electrode is melted while supplying the tin ions, and the steel sheet is plated, but the current efficiency is 100%. Since the tin concentration in the plating solution increases as the operation time increases due to the absence of the plating solution, it is necessary to adjust the concentration of the plating solution.
However, when the concentration of the plating solution is adjusted, it is necessary to adjust the concentration of a chemical solution other than tin, which is costly.
Therefore, an increase in the tin concentration in the plating solution has been prevented by changing the part of the self-fluxing tin electrode into an insoluble electrode and performing the plating treatment.

By the way, as mentioned above, in the production line of the tin-plated steel plate using a self-fluxing tin electrode, since a self-fluxing tin electrode is consumed with time, it is necessary to replace or replenish the self-fluxing tin electrode.
If the travel of the steel plate is stopped for replacement or replenishment of the self-fluxing tin electrode, the productivity will be lowered. Therefore, a self-fluxing tin electrode is provided with a hook-like engagement portion and is installed in a horizontal shape (tubular) It is possible to easily support and detach (hang down) by engaging with the locking member, and to replace and replenish without stopping the running of the steel plate.

  For this reason, in order to prevent the tin concentration in the plating solution from increasing by replacing the self-fluxing tin electrode with the insoluble electrode as described above, an engaging portion is provided on the insoluble electrode to lock the insoluble electrode. It is supported by engaging with a member.

JP 2006-348354 A

As described above, when the self-fluxing tin electrode and the insoluble electrode are provided with an engaging portion and engaged with the rod-shaped locking member to support the electrode, the self-fluxing tin electrode, the insoluble electrode and the locking member Must be electrically connected to each other, and power must be supplied to the self-soluble tin electrode and the insoluble electrode via the locking member.
Since the insoluble electrode gradually wears away from the contact portion with the locking member as the usage time increases, when power is supplied in a state where the contact portion with the locking member is worn, the insoluble electrode and the locking member Discharge occurs between the two. Therefore, it is necessary to replace or repair the insoluble electrode. However, since the insoluble electrode is made of platinum or the like as a material, there is a problem that the repair cost becomes high.

  An object of the present invention is to eliminate the above-described problems of the prior art, and in an electroplated steel sheet manufacturing apparatus using self-fluxing electrodes, plating is performed by disposing insoluble electrodes in order to adjust the ion concentration in the plating solution. An object of the present invention is to provide an apparatus for producing an electroplated steel sheet that facilitates repair of a worn insoluble electrode and enables repair of only the worn portion, thereby reducing the repair cost.

  In order to achieve the above object, the present invention provides an apparatus for producing an electroplated steel sheet that performs electroplating on a steel sheet that runs continuously in a plurality of plating cells that are arranged along a pass line and filled with a plating solution. At least one part that is immersed in a plating solution in the plating cell, arranged facing the steel plate, and continuously electroplated on the running steel plate while being energized and melted between the steel plate. At least one of the self-fluxing electrode and at least a part of which is immersed in a plating solution in the plating cell, arranged facing the steel plate, energized between the steel plate and continuously electroplating the traveling steel plate. Two insoluble electrodes and a plurality of locking members that are respectively suspended from the self-soluble electrode and the insoluble electrode and electrically connected to the self-soluble electrode and the insoluble electrode. An electroplated steel sheet comprising: a main body portion that is engaged with the engaging member, and a contact portion that is electrically connected, wherein the main body portion and the contact portion are detachable. A manufacturing apparatus is provided.

Here, it is preferable that a plurality of self-fluxing electrodes are arranged in the width direction orthogonal to the conveying direction of the steel sheet.
Moreover, it is preferable that a plurality of insoluble electrodes are arranged in the width direction orthogonal to the conveying direction of the steel plate, and the surfaces of the main body portions of the plurality of insoluble electrodes facing the steel plate are formed on the same plane parallel to the steel plate.
Moreover, a locking member is a rod-shaped member extended in the width direction orthogonal to the conveyance direction of a steel plate, and it is preferable to incline with respect to the surface of a steel plate.

Moreover, it is preferable that at least the surface of the insoluble electrode is made of platinum.
The insoluble electrode preferably has a fixing member that fixes the main body and the contact portion, and at least the surface of the fixing member is preferably made of the same material as the surface of the main body.

The insoluble electrode is preferably disposed in a plating cell in which the self-fluxing electrode is not disposed.
Moreover, it is preferable to have a circulating means for circulating the plating solution in the plurality of plating cells.

  According to the present invention, the insoluble electrode is formed so that the contact portion with the locking member is detachable, so that even when the contact portion with the locking member is worn, only the worn portion is repaired. Therefore, it can be easily repaired, and the repair cost of the insoluble electrode in which an expensive material such as platinum is used can be reduced.

It is a figure which shows notionally an example of the manufacturing apparatus of the electroplated steel plate which concerns on this invention. It is a schematic sectional drawing which shows the plating path | pass with the self-fluxing electrode and steel plate of the manufacturing apparatus of the electroplating steel plate shown in FIG. It is a schematic sectional drawing which shows the plating path | pass with the insoluble electrode and steel plate of the manufacturing apparatus of the electroplated steel plate shown in FIG. FIG. 4 is a side view of the plating pass shown in FIG. 3. (A) is the elements on larger scale which looked at the insoluble electrode shown in FIG. 4 from the a direction, (B) is the BB sectional drawing of (A).

  Below, the manufacturing apparatus of the electroplating steel plate which concerns on this invention is demonstrated in detail with reference to suitable embodiment shown to an accompanying drawing.

In FIG. 1, an example of the manufacturing apparatus of the electroplating steel plate of this invention is shown notionally.
The electroplated steel sheet manufacturing apparatus shown in FIG. 1 is also used as an electrotin-plated steel sheet or an electrotin-plated steel sheet manufacturing line called ETL (Electrolytic Tinning Line), such as a transport roll driven by a drive source (not shown). (Not shown) for carrying out electroplating such as electrotin plating on the traveling steel plate 11 continuously, and a plurality of platings continuously arranged so as to constitute an electroplating line Has a cell.
In the following description, the case of electrotin plating will be described as a specific representative example, but the present invention is not limited to this, and any electroplating using a self-fluxing electrode and an insoluble electrode can be used. Applicable. For example, in addition to tin plating, zinc plating, nickel plating, and the like can be given.

The electroplated steel sheet manufacturing apparatus 10 to which the present invention is applied is a plating section for performing an electroplating process. The line speed, the plate thickness and width of the plated steel sheet, and the current applied to the anode 30 Etc. are not particularly limited.
Further, in each plating cell 12, the formation of the plating path 34 can be eliminated by pulling up the anode 30, but the energization to the anode 30 disposed facing the steel plate 11 is selectively stopped. Thus, the function of the plating path 34 is selectively eliminated, and the plating on the surface of the steel plate 11 can be selectively stopped.

  The electroplated steel plate manufacturing apparatus 10 includes a plating cell 12b on the most upstream side in the conveying direction of the steel plate, a plurality of plating cells 12a on the downstream side of the plating cell 12b, and a plating solution 22 in the plating cells 12 (12a, 12b). And a pump 16 for feeding the plating solution 22 from the circulation tank 14 to the plating cell 12 (12a, 12b).

  Each of the plating cells 12a is disposed on a plating tank 20 filled with a plating solution 22, an immersion roll 24 that is immersed in the plating solution 22 and transports the steel plate 11, and an upper portion of the side wall portion 20a of the plating tank 20. A transport roll 26 that transports the steel plate 11, an energizing roll 28 that is in electrical contact with the steel plate 11 and energized, and an anode (anode) whose lower part is immersed in the plating solution 22 and that faces the steel plate 11. ) 30 and a DC power source (not shown) for supplying power between each anode 30 and each energizing roll 28 in each plating cell 12a.

The plating tank 20 stores therein a plating solution 22 such as a tin plating solution, and an anode (anode) composed of a dipping roll 24 and a plurality of self-fluxing electrodes 40 inside the plating solution 22. 30 are arranged.
The immersion roll 24 is a transport roll that is immersed in the plating solution 22 in the plating tank 20, winds the steel plate 11 that enters the plating solution 22 from above and travels downward, and conveys it vertically upward.

The transport rolls 26 are respectively arranged on the upper portions of the side wall portions 20a of the two adjacent plating tanks 20, wound around the steel plate 11, and from the immersion roll 24 in the upstream plating tank 20, into the downstream plating tank 20. It is a conveyance roll conveyed to the immersion roll 24.
The energizing roll 28 is a roll for electrically contacting and energizing the steel sheet 11 that is wound around and conveyed by each of the conveying rolls 26 so that the steel sheet 11 functions as a cathode.

  The anode 30 is immersed in the plating solution 22 in the plating tank 20, and is transported by the steel plate 11 transported by the upstream transport roll 26 and the immersion roll 24, and by the immersion roll 24 and the downstream transport roll 26. The steel plates 11 are arranged to face the front and back surfaces of the steel plates 11 so as to be spaced apart from each other by a predetermined distance, and are energized between the steel plates 11 serving as cathodes to form plating paths 34.

  Here, in each plating cell 12a in the illustrated example, the anode 30 is disposed to face the front and back surfaces of the steel plate 11 conveyed in the plating solution 22 in the plating tank 20, and one surface of the steel plate 11 is disposed. The anode 30 forms one plating path 34 for electroplating such as tin plating. That is, the plating path 34 formed in each plating cell 12 in the illustrated example is formed by the front and back surfaces of the steel plate 11 conveyed by the upstream conveying roll 26 and the immersion roll 24 and the anode 30 facing each surface. And two up paths formed by the front and back surfaces of the steel plate 11 conveyed by the immersion roll 24 and the downstream conveyance roll 26 and the anode 30 facing each surface.

FIG. 2 shows a plating path 34 between the anode 30 (anode) and the steel plate 11 in the plating cell 12a.
The plating pass 34 includes a steel plate 11 and anodes 30 disposed on both surfaces of the steel plate 11. The plating pass 34 a formed from the anode 30 a disposed on the lower surface side of the steel plate 11 in the drawing, and the upper surface side of the steel plate 11. The plating path 34b is composed of the anode 30b disposed on the surface. Since the plating pass 34a and the plating pass 34b have the same configuration, the plating pass 34a will be described as a representative example.

  As shown in FIG. 2, the anodes 30a of the plating path 34a are arranged on the lower surface side of the steel plate 11, and each of the anodes 30a is arranged in the width direction perpendicular to the traveling direction of the steel plate 11, for example, six in the illustrated example. Self-fluxing electrode 40 (40a to 40f) and a locking member (feeder bar) 38 for locking the self-fluxing electrode 40.

The self-fluxing electrode 40 is a rod-shaped member formed of a plating metal such as tin. The self-fluxing electrode 40 has a hook (a hook-shaped portion) on the upper part, and a part of the plating solution 22 is obtained by hooking the hook on the locking member 38. It is supported by the locking member 38 in a state where it is dipped in and suspended.
The self-fluxing electrode 40 is electrically connected to the locking member 38 and is supplied with electric power from a DC power source (not shown) via the locking member 38. Thereby, it supplies with electricity to the steel plate 11 conveyed in the plating solution 22, elutes the plating metal such as tin (plating metal ion such as tin ion) from itself, and the steel plate 11 in contact with the plating solution 22 Electrodeposition is performed on the front and back surfaces and plating is performed.

The locking member 38 is a rod-shaped member for locking the self-fluxing electrode 40, and has a predetermined inclination angle with respect to the surface of the steel plate 11, with the width direction of the steel plate 11 as the longitudinal direction above the plating tank 20. It is arranged at an angle. The locking member 38 has a substantially rectangular cross section perpendicular to the longitudinal direction, and the upper surface in the vertical direction is inclined downward in a direction away from the steel plate 11 (see FIG. 4).
Further, a direct current power source (not shown) is connected to the locking member 38 and power is supplied from the direct current power source.

As described above, when electroplating is performed using the self-fluxing electrode 40, the self-fluxing electrode 40 is consumed over time, and thus it is necessary to replace or replenish the self-fluxing electrode 40. If the travel of the steel plate 11 is stopped for the replacement or replenishment of the electrode 40, the productivity is lowered.
On the other hand, the self-fluxing electrode 40 is divided into a plurality of parts in the width direction, hooks are formed on the respective electrodes, and the self-fluxing electrode 40 is supported by being latched by a rod-shaped latching member 38. By adopting the structure, even when the steel plate 11 is traveling, a part of the self-fluxing electrode 40 can be attached and detached at both ends of the self-soluble electrode 40. Therefore, replacement and replenishment can be performed without stopping the traveling of the steel plate 11. can do.

Specifically, replacement and replenishment of the self-fluxing electrode 40 will be described using the lower plating pass 34a in FIG.
Among the self-fluxing electrodes 40 (40a to 40f) of the anode 30a of the plating pass 34a, when the self-fluxing electrode 40a at the left end in the figure has a preset thickness to be extracted, the left-most self-dissolving electrode 40a is extracted and the right side thereof The remaining self-dissolving electrodes 40b to 40f are moved to the left by the electrode width. A new self-fluxing electrode 40 is attached to the vacant region at the right end, and an anode 30 a is newly formed by the six self-fluxing electrodes 40.
In this way, the anode 30a is formed with a plurality of self-fluxing electrodes 40, the thin self-fluxing electrode 40 is extracted from one end side, and the remaining self-fluxing electrodes 40 are sequentially moved to obtain a new self-fluxing electrode 40. Since it replaces and replenishes the self-fluxing electrode 40 by attaching to the other end side, it is not necessary to stop the travel of the steel plate 11, and it is possible to prevent the productivity from decreasing.

The plating cell 12b is disposed on the upstream side of the plurality of plating cells 12a.
The plating cell 12b has the same configuration as the plating cell 12a except that an insoluble electrode 42 is disposed instead of the self-fluxing electrode 40. Therefore, the same reference numerals are given to the same members, and the following description is different. Mainly.

  The plating cell 12b is respectively disposed on the plating tank 20 filled with the plating solution 22, the immersion roll 24 that is immersed in the plating solution 22 and transports the steel plate 11, and the upper portion of the side wall portion 20a of the plating tank 20. A transport roll 26 that transports the steel plate 11, an energizing roll that is in electrical contact with the steel plate 11, and an anode (anode) 32 that is immersed in the plating solution 22 and faces the steel plate 11. A direct current power source (not shown) for supplying electric power between the anode 32 and the energizing roll 28 in the plating cell 12b.

  The anode 32 is immersed in the plating solution 22 in the plating tank 20 and is arranged at a predetermined distance from the back surface of the steel plate 11 conveyed by the immersion roll 24 and the downstream conveyance roll 26 to become a cathode. The plating path 36 is formed by energizing the steel plate 11.

FIG. 3 shows a plating path 36 between the anode 32 and the steel plate 11 in the plating cell 12b. In FIG. 3, the upper side in the drawing is illustrated as the back surface of the steel plate 11.
The plating path 36 is formed from the steel plate 11 and the anode 32 disposed on the back surface of the steel plate 11.
As shown in FIG. 3, the anode 32 of the plating path 36 is arranged on the back surface side of the steel plate 11 and has a plurality of, in the illustrated example, six insoluble electrodes 42 (42 a to 42 f) arranged in the width direction of the steel plate 11. And a locking member (feeder bar) 38 for locking the insoluble electrode 42.

4 shows a side view of the plating path 36, FIG. 5A shows a partially enlarged view of the insoluble electrode 42 of FIG. 4 viewed from the direction a, and FIG. -B line sectional drawing is shown.
The insoluble electrode 42 is a rod-shaped member, and has a main body portion 44 having a maximum surface facing the steel plate 11, a contact portion 46 that is locked to the locking member 38, and a fixing that fixes the main body portion 44 and the contact portion 46. It has a bolt 48, a nut 50, and a washer 52, which are members.

The main body 44 is a rod-like member whose base material is titanium and whose surface is plated with platinum. The main body portion 44 is arranged with the maximum surface facing the back surface of the steel plate 11 and the longitudinal direction being aligned with the vertical direction.
As shown in FIGS. 5A and 5B, the contact portion 46 is fixed to the surface of the main body 44 opposite to the surface facing the steel plate 11. A through hole 44a through which a bolt 48 for fixing the contact portion 46 passes is formed at a position where the contact portion 46 is fixed. Further, a through-hole 44b that engages with a jig for handling the insoluble electrode 42 when the insoluble electrode 42 is engaged with the locking member 38 is formed on the upper end of the main body 44 in the longitudinal direction.

  Moreover, as shown in FIG. 3, the main-body part 44 is formed in different thickness according to the arrangement position of the width direction. That is, as shown in the figure, since the locking member 38 is installed to be inclined with respect to the steel plate 11, the surfaces of the insoluble electrodes 42a to 42f facing the steel plate 11 are parallel to the steel plate 11 and the same. The main body portion 44 of the insoluble electrode 42a disposed at a position close to the steel plate 11 is formed so as to be thin on the surface, and the main body portion 44 of the insoluble electrode 42f disposed at a position far from the steel plate 11 is thick. The insoluble electrodes 42b to 42e that are formed and arranged between them are formed so that the main body 44 is thicker as the insoluble electrodes 42b to 42e are arranged farther from the steel plate 11.

The contact portion 46 is a plate-like member whose base material is titanium and whose surface is plated with platinum, and is fixed to the surface of the main body portion 44 opposite to the surface facing the steel plate 11. Further, a through hole 46 a through which a bolt 48 for fixing the contact portion 46 to the main body portion 44 passes is formed on the surface in contact with the main body portion 44.
Further, the surface on the lower side in the vertical direction of the contact portion 46 is inclined downward in a direction away from the steel plate 11, and forms a hook-like portion (hook) together with the main body portion 44, and this hook-like portion is a locking member. The insoluble electrode 42 is suspended and supported, and is electrically connected to the locking member 38.

The bolt 48, the nut 50, and the washer 52, which are fixing members that fix the main body 44 and the contact portion 46, are formed by plating a surface of a base material made of titanium with platinum.
Thus, by making the surface of the fixing member that fixes the main body portion 44 and the contact portion 46 the same as the material of the surface of the main body portion 44, the electrical characteristics of the insoluble electrode 42 are changed between the main body portion and the contact portion. Can be equivalent to an insoluble electrode formed integrally.

The insoluble electrode 42 engaged with the locking member 38 is electrically connected to the locking member 38 and supplied with electric power from a DC power source (not shown) via the locking member 38. Thereby, the steel strip 11 conveyed in the plating solution 22 is energized, and tin ions in the plating solution 22 are electrodeposited on the back surface of the steel plate 11 in contact with the plating solution 22 to perform the plating process.
As described above, in the plated steel sheet production line using the self-fluxing electrode 40, the concentration of tin (plating metal) in the plating solution 22 increases as the operating time increases, so the insoluble electrode 42 is installed in the line. The insoluble electrode 42 is used as the anode 32 to perform plating, and the tin ions in the plating solution 22 are consumed, thereby preventing the tin concentration in the plating solution 22 from increasing.

  Here, as described above, when the insoluble electrode is provided with a hook-like portion and engaged with the rod-shaped locking member 38 to support the insoluble electrode, the insoluble electrode has a locking member as the usage time increases. 38, in the illustrated example, the lower surface of the contact portion that contacts the upper surface of the locking member 38 gradually wears, so when power is supplied while the contact portion with the locking member 38 is worn. A discharge occurs between the insoluble electrode and the locking member 38. Therefore, it is necessary to replace or repair the insoluble electrode. However, the insoluble electrode is very expensive because platinum or the like is used as a material. If the entire insoluble electrode is replaced, the repair cost becomes high. It was.

On the other hand, in the present invention, the insoluble electrode 42 is formed by the main body portion 44 facing the steel plate 11 and the contact portion 46 that is engaged with and electrically connected to the locking member 38. By fixing the contact portion 46 so as to be detachable, even when the contact portion with the locking member 38 is worn, it is possible to replace only the contact portion 46 that has come into contact with the locking member 38 and is insoluble. The electrode 42 can be easily repaired, and the repair cost of the insoluble electrode 42 in which an expensive material such as platinum is used can be reduced.
In addition, when the insoluble electrode 42 and the locking member 38 are locked, the area in contact with the upper surface of the locking member 38 is subjected to the weight of the insoluble electrode 42 and the pressure is increased, so that wear due to contact increases. Therefore, it is preferable that at least a region in contact with the upper surface of the locking member 38 is the contact portion 46.

Here, in the illustrated example, one anode 32 made of the insoluble electrode 42 is disposed in the plating cell 12b on the most upstream side, but the present invention is not limited to this, and two or more anodes 32 are disposed. Also good.
Further, the configuration includes one plating cell 12b in which the anode 32 made of the insoluble electrode 42 is disposed. However, the present invention is not limited to this, and there are two or more plating cells 12b in which the anode 32 made of the insoluble electrode 42 is disposed. May be.

Moreover, although the plating cell 12b was arrange | positioned in the upstream of the some plating cell 12a by which the anode 30 which consists of the self-fluxing electrode 40 is arrange | positioned, it is not limited to this, You may arrange | position between the plating cells 12a. However, it may be arranged downstream of the plating cell 12a.
In the illustrated example, the anode 32 made of the insoluble electrode 42 is arranged in a plating cell 12b different from the plating cell 12a in which the anode 30 made of the self-fluxing electrode 40 is arranged, but this is not limitative. Instead, the anode 32 made of the insoluble electrode 42 and the anode 30 made of the self-soluble electrode 40 may be disposed in the same plating cell.
Further, in the illustrated example, the electrodes in the width direction in one anode are all either the insoluble electrode 42 or the self-soluble electrode 40, but the insoluble electrode 42 and the self-soluble electrode 40 are provided in one anode. It may be mixed. However, considering the ease of replacement of the self-fluxing electrode and the difference in the electrodeposition state, it is preferable to use separate anodes.
In addition, the number of the insoluble electrodes 42 to be arranged may be appropriately determined in consideration of the balance between the amount of plating component dissolved from the self-soluble electrode and the amount of electrodeposition.

Further, in the illustrated example, the anode 32 made of the insoluble electrode 42 is disposed in the up path on the back surface side of the steel plate 11, but is not limited thereto, and may be disposed on the front surface side of the steel plate 11, It may be arranged in the down path.
Moreover, in FIG. 3, although the example which consists of several electrodes (42a-42f) divided | segmented into the width direction as the insoluble electrode 42, and having different thickness according to the arrangement position of the width direction was shown, this is insoluble. This is a preferred mode for enabling the installation position of the electrode 42 to be fluidly selected and diverting the mounting jig (locking member 38) for the self-soluble electrode 40 as it is. However, when fixing the position of the insoluble electrode 42, it is not necessary to divert the mounting jig for the self-soluble electrode 40, and it is only necessary to install a mounting jig (locking member) for the insoluble electrode 42. It is not necessary to change the thickness according to the arrangement position in the width direction, and the surface of the insoluble electrode 42 that faces the steel plate 11 is parallel to the steel plate 11 and arranged on the same surface. Good. In FIG. 3, the number of divisions is six in the width direction, but the number of divisions is not particularly limited and may not be divided.

In this embodiment, the main body portion 44 and the contact portion 46 of the insoluble electrode 42 are formed by plating platinum on the surface using titanium as a base material. However, the present invention is not limited to this, and the whole is made of platinum. Also good.
In addition, although the surface material is platinum, the present invention is not limited thereto, and various metals used as insoluble electrodes can be applied. For example, a metal such as iridium may be used. Moreover, although the material of the base material is titanium, the material is not limited to this. For example, a metal such as stainless steel (SUS) may be used.

The circulation tank 14 is connected to all the plating cells 12 (12 a, 12 b), and as shown by arrows in FIG. 1, the plating solution 22 flows from each plating cell 12, and each plating cell is connected via a pump 16. The plating solution 22 is supplied to 12 and the plating solution overflowed from the upper part of each cell is returned to the circulation tank 14 (not shown), whereby the plating solution 22 is circulated.
Further, in the circulation tank 14, the plating solution 22 flowing from each plating cell 12 may be agitated. Further, the concentration of the chemical solution in the plating solution 22 may be adjusted.
By circulating the plating solution 22 in the plating cell 12, tin ions (plating metal ions) in the plating solution 22 are consumed by the plating cell 12 b having the insoluble electrode 42. Therefore, the plating cell 12 a having the self-fluxing electrode 40. It is possible to prevent the concentration of tin ions in the plating solution 22 from increasing.

  The flow rate of the plating solution 22 between the circulation tank 14 and each plating cell 12 is not particularly limited, as long as the tin concentration and the chemical concentration of the plating solution 22 in each plating cell 12 are maintained within a predetermined range. Good.

  Moreover, in the said Example, although it was set as the structure which circulates the plating solution 22 of all the plating cells 12 (12a, 12b) with the circulation tank 14 and the pump 16, this invention is not limited to this, One A configuration in which the anode 30 composed of the self-soluble electrode 40 and the anode 32 composed of the insoluble electrode 42 are arranged in the plating cell to prevent the concentration of the plating metal ions in the plating solution 22 from increasing in one plating cell. It is good.

  As mentioned above, although the manufacturing apparatus of the electroplating steel plate which concerns on this invention was described in detail, giving the embodiment and the example by tin plating specifically, this invention is not limited to the above embodiment and an Example. Of course, various improvements and modifications may be made without departing from the scope of the present invention.

DESCRIPTION OF SYMBOLS 10 Electroplating steel plate manufacturing apparatus 11 Steel plate 12a, 12b Plating cell 14 Circulation tank 16 Pump 20 Plating tank 22 Plating solution 24 Immersion roll 26 Transport roll 28 Current supply roll 30a, 30b, 32 Anode (anode)
34a, 34b, 36 Plating pass 38 Locking member (feeder bar)
40, 40a, 40b, 40c, 40d, 40e, 40f Self-dissolving electrode 42, 42a, 42b, 42c, 42d, 42e, 42f Insoluble electrode 44 Body 44a, 44b, 46a Through hole 46 Contact part 48 Bolt 50 Nut 52 Washer

Claims (8)

In an electroplated steel sheet manufacturing apparatus that performs electroplating on a steel sheet that is disposed along a pass line and continuously travels in a plurality of plating cells filled with a plating solution,
At least a portion is immersed in a plating solution in the plating cell, arranged facing the steel plate, and continuously electroplated on the traveling steel plate while being energized and melted between the steel plate. At least one self-fluxing electrode;
At least one part that is immersed in a plating solution in the plating cell, arranged facing the steel plate, energized between the steel plate, and continuously electroplates the traveling steel plate. An insoluble electrode;
The self-fluxing electrode and the insoluble electrode are respectively suspended, and includes a plurality of locking members electrically connected to the self-fluxing electrode and the insoluble electrode,
The insoluble electrode has a main body portion whose maximum surface faces the steel plate, a contact portion that is locked to the locking member and electrically connected, and the main body portion and the contact portion are An apparatus for producing an electroplated steel sheet, which is detachably formed.   The said self-fluxing electrode is a manufacturing apparatus of the electroplating steel plate of Claim 1 arrange | positioned in the width direction orthogonal to the conveyance direction of the said steel plate.   A plurality of the insoluble electrodes are arranged in the width direction orthogonal to the conveying direction of the steel plate, and the surfaces of the main body portions of the plurality of insoluble electrodes facing the steel plate are formed on the same plane parallel to the steel plate. The apparatus for producing an electroplated steel sheet according to claim 1 or 2.   The said latching member is a rod-shaped member extended in the width direction orthogonal to the conveyance direction of the said steel plate, and is inclined and arrange | positioned with respect to the surface of the said steel plate. Electroplated steel plate manufacturing equipment.   The apparatus for producing an electroplated steel sheet according to any one of claims 1 to 4, wherein the insoluble electrode has at least a surface made of platinum.   The said insoluble electrode has a fixing member which fixes the said main-body part and the said contact part, The at least surface of the said fixing member consists of the same material as the surface of the said main-body part. Electroplated steel plate manufacturing equipment.   The said insoluble electrode is a manufacturing apparatus of the electroplating steel plate in any one of Claims 1-6 arrange | positioned in the plating cell in which the said self-fluxing electrode is not arrange | positioned.   The apparatus for producing an electroplated steel sheet according to any one of claims 1 to 7, further comprising circulating means for circulating a plating solution in the plurality of plating cells.

Images