KR20060103358A - A fabrication device and method of a continuous metal mesh by cathode drum electrodeposition process - Google Patents

Abstract

The present invention relates to an apparatus and method for manufacturing a continuous metal mesh by a mesh-type rotating cathode drum plating method, comprising: an electrolytic cell 100 containing an electrolyte solution; A part of the mesh type cathode drum 200 installed to be immersed in the electrolyte of the electrolytic cell 100 and rotating with an applied power; An anode basket (300) installed to be completely immersed in the electrolyte of the electrolytic cell (100) and formed in a shape corresponding to the mesh type cathode drum (200) and maintaining a predetermined distance; It is provided on one side of the electrolytic cell 100, consisting of an electrolytic solution spraying means 400 for spraying the electrolytic solution so that the electrolytic solution of the electrolytic cell 100 is stirred; Electrolyte solution is sprayed by the applied power supply and the electrolytic solution stirring step (S11) for stirring the electrolytic solution of the electrolytic cell 100, and the electrolytic solution stirred in the electrolytic solution stirring step (S11) is continuously plated on the surface of the mesh-type cathode drum 200 Peeling the metal mesh (M) to be plated on the surface of the mesh-type cathode drum 200 through the cathode drum rotation step (S12) and the cathode drum rotation step (S12) so as to rotate the mesh-type cathode drum (200) so that It comprises a peeling step (S13), and the winding step (S14) for winding the metal mesh (M) to be peeled off in the peeling step (S13). According to such a configuration, there is an advantage of mass production of high quality metal mesh having a wide and long length.

Continuous, Cathodic Drum Plating, Metal Mesh, Electrolyzer, Mesh Cathode Drum, Anode Basket

Description

A fabrication device and method of a continuous metal mesh by cathode drum electrodeposition process}

1 is a schematic configuration diagram of an apparatus for manufacturing a continuous metal mesh by a mesh-type rotating cathode drum plating method according to a preferred embodiment of the present invention.

2 is a perspective view of a mesh type cathode drum which is a main component of a continuous metal mesh production apparatus by a mesh type rotating cathode drum plating method according to a preferred embodiment of the present invention.

3 is a partial perspective view of an electrolytic cell showing a state in which the mesh-type cathode drum is removed from the continuous metal mesh production apparatus by the mesh-type rotating cathode drum plating method according to the preferred embodiment of the present invention.

Figure 4 is a schematic process flow diagram of a method of manufacturing a continuous metal mesh by the mesh-type rotary cathode drum plating method according to a preferred embodiment of the present invention.

Figure 5 is a surface photograph of the nickel mesh produced by the continuous metal mesh production apparatus and manufacturing method by the mesh-type rotary cathode drum plating method of the present invention.

Explanation of symbols on the main parts of the drawings

100. ..... electrolytic cell 120. ..... auxiliary tank

200. ..... Mesh type cathode drum 220. ..... Rotating shaft

240. ..... Drum 242. ..... Mesh

260. ..... Motor 280. ..... Chain

300. ..... Positive basket 320. ..... Drum housing

340. ..... Clusters 360. ..... Breakaway prevention network

380. ..... Metal Cluster 390. ..... Anode Power Supply

400. ..... electrolyte injection means 420. ..... pipe

440. ..... electrolytic injection hole 500. ..... circulation-filtering means

520. ..... First connector 540. ..... Second connector

600. ..... Guide Roller B. ..... Busbar

M. ..... Metal Mesh S11. ..... Electrolyte Stirring Step

S12. ..... Cathode drum rotation step S13. ..... Peeling step

S14. ..... winding stage

The present invention relates to a manufacturing apparatus and a manufacturing method according to the cathode drum plating method, and more particularly, the anode is made of a mesh-type cathode drum and the insoluble anode, the surface is directly processed into a mesh form or the mesh is attached to the surface The mesh-type rotary cathode drum is formed by the mesh-type cathode drum and the anode basket, while the electrolyte is agitated by the injection of the electrolyte while maintaining a constant distance, and the mesh-type cathode drum is rotated to plate the metal on the surface thereof. It relates to a continuous metal mesh production apparatus and a manufacturing method.

In general, as a method of manufacturing a metal thin plate, a continuous casting method using a double roll, a melt spinning method, and a rolling method are used.

The manufacture of thin plates using continuous casting is currently producing up to a few millimeters of thickness of hot rolled sheet, but the manufacture of ultra-thin plates has not been successful. This method allows the process atmosphere to be controlled by argon (Ar) gas during the manufacturing process. Therefore, at this time, due to gas bubbles, manufacturing problems such as surface defects of the metal thin plate and surface layer destruction due to overheating occur.

Melt spinning method is one of the manufacturing method of the thin plate through rapid solidification, it is advantageous to obtain a relatively uniform thin plate by manufacturing a metal thin plate by spraying molten metal on a rotating cooling roll.

However, in order to manufacture a thin plate of uniform composition, it is restricted to perform the work in a vacuum state, and the method developed to overcome this has been made possible by working in the air by the Planar Flow Casting (PFC) method. There is a problem that the deviation is severe.

Rolling method, which is the most popular method, has many advantages in the production of thin plates, but not only the manufacturing cost increases due to the numerous steps of rolling, but also the production of ultra-thin plates (thickness of 30 μm or less) leads to an increase in product cost. There is a limit to the application.

For example, as disclosed in US Pat. No. 4948434, in order to manufacture a metal sheet having a thickness of about 100 μm or less, multistage rolling and annealing should be performed. The multi-stage cold rolling process has a problem that the yield is less than 30% due to complex, difficult and long time-consuming disadvantages, and problems such as uneven shape, thickness variation, edge crack, etc., and also high manufacturing cost. .

Recently, many researches have been conducted on a method of manufacturing a thin plate using electroplating. The metal sheet manufacturing method disclosed in Korean Patent Publication No. 1999-0064747 uses the same electrocycle method as the present invention.

However, in this manufacturing apparatus, a separate electrolyte supply means does not exist, and since the electrolyte is agitated simply by using a paddle, the concentration distribution of the electrolyte is not uniform, and numerous bubbles are caused by the vertical movement or the horizontal movement of the rod-shaped paddle. There is a disadvantage of generating. Since this stirring method is not suitable for the production of alloy thin plates requiring a uniform composition, it is necessary to introduce a new production method.

Nickel (Ni), a ferromagnetic material, has excellent performance (E-Field, H-Field) as an electromagnetic shielding material, and is used close to the human body such as mobile communication equipment such as mobile phones, PDAs, and notebook computers. It is known to be effective for shielding the electromagnetic wave of IT products, which are used in various forms in the form of thin plates or meshes. In particular, the mesh has been applied to various fields by having a ventilation function for heat generated from electronic components as well as electromagnetic shielding characteristics.

Until now, metal mesh is manufactured by using weaving method of metal wire applied in Germany, etc. and polyester (Polyester) developed in Japan, and manufacturing metal mesh using electroless plating method. There is a method, in the case of such a woven mesh has a disadvantage that the size of the hole (Hole) is large, the portion occupied by the wire (Wire) is small, it is difficult to manufacture in the form of a thin film.

The method developed to compensate for this is to produce a mesh by etching the thin plate and then use the electroplating method to produce the desired metal mesh, which is mainly batch type. ), And the batch type has a disadvantage in that the production cost is high because the work process has to be complicated and expensive.

Therefore, an object of the present invention for solving the above problems, the mesh-type rotating cathode is provided with a positive electrode basket consisting of a mesh-type cathode drum and an insoluble anode, the surface is directly processed into a mesh form or the mesh is attached to the surface An apparatus for producing a continuous metal mesh by a drum plating method is provided.

Another object of the present invention is a mesh-type rotating cathode drum configured to spray and stir an electrolyte solution into an electrolyte of an electrolytic cell, and to rotate the mesh-type cathode drum while maintaining a constant distance from the anode basket so that metal is plated on the surface of the mesh-type cathode drum. It is to provide a continuous metal mesh manufacturing method by the plating method.

An apparatus for producing a continuous metal mesh by the mesh-type rotating cathode drum plating method of the present invention for achieving the above object includes an electrolytic cell containing an electrolyte; A mesh type negative electrode drum installed to be partially immersed in the electrolytic solution of the electrolytic cell and rotating with an applied power source; An anode basket installed to be completely immersed in the electrolyte of the electrolytic cell, the anode basket being formed in a shape corresponding to the mesh type cathode drum and maintaining a predetermined distance; An auxiliary tank formed at a lower portion of the electrolytic cell to receive an electrolyte flowing from the electrolytic cell; An electrolytic solution spraying means installed at one side of the electrolytic cell and spraying the electrolytic solution so that the electrolytic solution of the electrolytic cell is stirred; Circulation-filtering means provided on one side of the auxiliary tank to remove foreign substances in the electrolyte while circulating the electrolyte in the auxiliary tank to the electrolytic cell; Winding means provided on one side of the mesh type cathode drum and winding a metal mesh formed on a surface of the mesh type cathode drum; It is provided on one side of the mesh-type cathode drum, characterized in that it comprises a cleaning means for cleaning the surface of the mesh-type cathode drum.

The mesh type cathode drum is characterized in that the surface can be directly processed into a mesh form or a mesh (Mesh) processed into a weaving type or a batch type can be attached to the surface.

The mesh on the surface of the mesh type cathode drum is made of a single metal or an alloy.

The anode basket is made of an insoluble anode.

The anode basket is formed in a circular arc shape cut in half, the drum receiving portion for receiving the mesh-type cathode drum; A cluster accommodating part formed at one side of the drum accommodating part and accommodating a metal cluster having the same component as the electrolyte of the electrolytic cell; A separation prevention net formed at an outer side of the cluster accommodating part and preventing separation of the metal cluster; It is formed on both ends of the drum receiving portion, characterized in that it comprises a positive power supply connected to the power applied.

The anode basket is made of titanium (Ti).

In addition, the method of manufacturing a continuous metal mesh by the mesh-type rotary cathode drum plating method of the present invention includes an electrolyte stirring step of stirring the electrolyte solution of an electrolytic cell by spraying an electrolyte solution with an applied power source, and an electrolyte solution stirred in the electrolyte stirring step of a mesh type cathode drum. A cathode drum rotation step of rotating the mesh-type cathode drum to be continuously plated on the surface of the, and a peeling step of peeling the metal mesh plated on the surface of the mesh-type cathode drum while the cathode drum rotation step, and peeling in the peeling step Characterized in that comprises a winding step of winding the metal mesh to be.

According to the method of manufacturing and manufacturing a continuous metal mesh by the method of the present invention, the male-type rotary cathode drum plating having such a configuration, there is an advantage of mass production of high-quality metal mesh having a wide and long length.

Hereinafter, with reference to the accompanying drawings, a preferred embodiment of the continuous metal mesh manufacturing apparatus and manufacturing method by the present invention mesh type rotary cathode drum plating method as described above will be described in detail.

Figure 1 is a schematic configuration diagram of a continuous metal mesh manufacturing apparatus by a mesh-type rotating cathode drum plating method according to a preferred embodiment of the present invention, Figure 2 is a mesh-type rotating cathode drum according to a preferred embodiment of the present invention A perspective view of a mesh type cathode drum, which is a main component of the continuous metal mesh manufacturing apparatus by the plating method, is shown. FIG. 3 illustrates a mesh type in the continuous metal mesh manufacturing apparatus using the mesh type rotary cathode drum plating method according to a preferred embodiment of the present invention. A partial perspective view of an electrolytic cell showing the state where the cathode drum is removed is shown.

And, Figure 4 is a schematic process flow diagram of a method of manufacturing a continuous metal mesh by the mesh-type rotary cathode drum plating method according to a preferred embodiment of the present invention, Figure 5 is a continuous process by the mesh-type rotary cathode drum plating method of the present invention The surface shape of the nickel mesh manufactured by the metal mesh manufacturing apparatus and the manufacturing method is shown.

As shown in these figures, the continuous mesh mesh manufacturing apparatus according to the present invention mesh-type rotary cathode drum plating method is immersed in the electrolytic cell 100 and the electrolyte of the electrolytic cell 100 to accommodate the electrolyte to be plated (沈) 메쉬) mesh-type negative electrode drum 200 which is installed to be rotated by an applied power source to be installed and completely immersed in the electrolyte of the electrolytic cell 100, and is formed in a shape corresponding to the mesh-type negative electrode drum 200 and has a predetermined distance. It is composed of a positive electrode basket 300 and the like to hold.

The electrolytic cell 100 is formed in a substantially square cylindrical shape, the electrolytic cell 100 is accommodated in the electrolyte to be plated on the surface of the mesh-type cathode drum 200. In addition, an auxiliary tank 120 is formed in the lower portion of the electrolytic cell 100 to receive the electrolyte flowing from the electrolytic cell 100. The structure in which the electrolyte is accommodated is composed of a double of the electrolytic cell 100 and the auxiliary tank 120. .

Therefore, a part of the rotating mesh type cathode drum 200, that is, about half, is immersed in the electrolytic cell 100, and the electrolytic solution of the electrolytic cell 100 is injected into the electrolytic solution spraying means 400 to be described below. The electrolyte is stirred, and the electrolyte flowing through the electrolytic cell 100 while being agitated by the electrolyte injection of the electrolyte injection means 400 is configured to be accommodated in the auxiliary tank 120.

The electrolytic cell 100 is provided with a mesh type cathode drum 200 which is immersed about halfway in the electrolyte. The mesh type cathode drum 200 is connected to the cathode (-) of the power applied to the cylindrical drum 240 having a constant width while surrounding the rotating shaft 220 and the rotating shaft 220 to be rotatable Is formed.

Although not shown at one end of the rotating shaft 220 is provided with a power supply for supplying a negative electrode (-) from the rectifier, the other end motor 260 for providing a rotational force to rotate the drum 240 and The chain 280 is coupled.

And, both ends of the electrolytic cell 100 coupled to the rotating shaft 220 is provided with a support (not shown) for inserting a bearing so that the rotating shaft 220 is smoothly rotated, the rotating shaft ( 220 is easily attached and detached to facilitate maintenance of the mesh type cathode drum 200.

As shown in FIG. 2, a mesh 242 having a shape to be manufactured is formed on the surface of the drum 240. The mesh 242 is formed in a mesh shape in which a plurality of hexagons are connected to each other, as if in a honeycomb form.

The mesh 242 may be composed of a single metal or an alloy according to the component of the electrolyte to be plated, and integrally with the mesh type cathode drum 200 by directly processing the surface of the mesh type cathode drum 200. By attaching to the surface of the mesh-type cathode drum 200, the mesh 242 processed in a weaving type or batch type formed by using as a weaving or weaving with a metal wire Could be used.

An anode basket 300 formed of an insoluble anode (+) is installed under the mesh type cathode drum 200. The anode basket 300 is formed so as to be immersed in the electrolyte of the electrolytic cell 100 and formed in an arc shape cut in half so as to correspond to the mesh type cathode drum 200 to maintain a constant distance.

As shown in FIG. 3, the anode basket 300 has a drum accommodating part 320 formed in an arc shape having a half cut in the center portion thereof. The drum accommodating unit 320 serves to accommodate the rotating cylindrical mesh type cathode drum 200, and is connected to the positive electrode (+) of the applied power to the surface of the mesh type cathode drum 200 Maintain a certain distance so that the plating.

Inside the drum accommodating part 320, a cluster accommodating part 340 is formed in which a metal cluster 380 having the same component as the electrolyte of the electrolytic cell 100 is accommodated. The cluster accommodating part 340 has a space recessed and molded into the anode basket 300 and is formed of the same curved surface as the drum accommodating part 320.

On the outside of the cluster accommodating portion 340, a departure prevention net 360 for preventing the separation of the metal cluster 380 is formed. The departure prevention net 360 is formed of a mesh having a size that does not pass through the metal cluster 380, the dissolution prevention net 360 is dissolved positive (+) ions of the metal cluster 380 By moving to the mesh 242 formed on the surface of the mesh-type cathode drum 200 and bonded to the component of the electrolyte on the mesh 242.

In addition, positive and negative power supply units 390 are connected to both ends of the drum accommodating unit 320 so as to be connected to the positive pole (+) of the applied power to supply electricity to the positive electrode basket 300. Four positive and negative power supply units 390 are formed at both front and rear sides thereof and are connected to a power source by contacting bus bars (B) provided at the bottom thereof.

On the other hand, since the positive electrode basket 300 is formed of an insoluble anode that is not dissolved in water as a whole, it is preferable that the positive electrode basket 300 is made of titanium (Ti) or a titanium alloy.

In addition, the metal cluster 380 accommodated in the cluster accommodating part 340 is dissolved in the electrolyte solution of the electrolytic cell 100 by the metal mass of the same component as the electrolyte of the electrolytic cell 100 of the mesh cathode cathode 200 It serves to match the amount and concentration of the electrolyte solution plated on the surface.

At the lower end of the electrolytic cell 100, more specifically, the center portion of the cluster portion 340 of the positive electrode basket 300 is provided with an electrolytic solution spraying means 400 for injecting an electrolytic solution so that the electrolytic solution of the electrolytic cell 100 is stirred. do. The electrolyte injection means 400 is formed of a cylindrical plastic pipe 420 having a long length in communication with the circulation-filtering means 500 to be described below, the electrolyte ions penetrated so that the electrolyte is injected into the pipe 420 A plurality of holes 440 is formed.

Accordingly, the mesh type by spraying the electrolyte solution of the electrolytic cell 100 to the electrolyte injection means 400 while stirring to smoothly remove the hydrogen (H ₂ ) gas generated from the mesh type cathode drum 200. A uniform plating layer is formed on the mesh 242 on the surface of the cathode drum 200.

The right side (in FIG. 1) of the auxiliary tank 120 is provided with circulation-filtering means 500 for removing foreign matter in the electrolyte while circulating the electrolyte in the auxiliary tank 120 to the electrolytic cell 100. The circulation-filtering means 500 includes a first connecting pipe 520 for guiding the electrolyte flowing from the auxiliary tank 120 and filtering the electrolyte flowing into the first connecting pipe 520. A second connecting pipe 540 for guiding the electrolyte solution, which is in communication with the electrolyte injection means 400, to the electrolytic cell 100 is coupled.

In addition, the upper portion of the mesh type cathode drum 200 is provided with a guide roller 600 for peeling the metal mesh (M) to be plated on the mesh 242 of the mesh type cathode drum 200, One side of the guide roller 600 is further provided with cleaning means (not shown) for cleaning the surface of the mesh-type cathode drum 200 in which the metal mesh (M) is peeled off.

In addition, although one side of the mesh type cathode drum 200 is not shown, winding means for winding the metal mesh M peeled off by the guide roller 600 is provided. The winding means may be formed in a roll shape to be configured to continuously wind the metal mesh (M) continuously peeled off from the guide roller (600).

Hereinafter, the operation of the apparatus for producing a continuous metal mesh by the mesh-type rotating cathode drum plating method configured as described above will be described with reference to FIG.

First, the electricity is supplied to the electrolytic solution of the electrolytic cell 100 by a power source applied so that electrolysis occurs, and the electrolytic solution is injected by the electrolytic solution spraying means 400 to the electrolytic cell 100. Stirring the electrolyte solution step (S11) proceeds.

Then, after the electrolytic solution stirring step (S11) proceeds, the mesh-type cathode drum 200 so that the electrolyte solution stirred in the electrolytic cell 100 is continuously plated on the surface of the mesh-type cathode drum 200, that is, the mesh 242. The cathode drum rotating step (S12) to rotate is in progress.

In the cathode drum rotating step S12, when the operation button (not shown) provided in the power supply device (not shown) is operated, the motor 260 is driven to rotate the rotating shaft of the mesh type cathode drum 200. As the chain 280 connected to the 220 rotates, the mesh type cathode drum 200 is rotated, and the rotating mesh type cathode drum 200 is formed on the mesh 242 formed on the surface thereof. The rotational speed is preferably controlled according to the size so that the plating layer is formed uniformly.

At this time, the electrolyte solution of the electrolytic cell 100 flows into the auxiliary tank 120 while being agitated by the electrolyte solution injected from the electrolyte injection means 400, and thus the electrolyte solution contained in the auxiliary tank 120 is the first connection pipe. 520 is introduced into the circulation-filtering means 500, and the electrolyte flowing into the circulation-filtering means 500 is filtered through the circulation-filtering means 500. By being guided to the electrolytic cell 100 through), the electrolytic solution insufficient in the electrolytic cell 100 is replenished.

After the cathode drum rotation step S12 is performed, the guide roller 600 is a metal mesh M plated on the mesh 242 on the surface of the mesh type cathode drum 200 while the cathode drum rotation step S12 is performed. Peeling step (S13) to be peeled in) is in progress. In the peeling step (S13), a process of cleaning the surface of the mesh type cathode drum 200 in which the metal mesh M is peeled off by the guide roller 600 is performed by the cleaning means.

After the peeling step S13 is performed, the winding step S14 for winding the metal mesh M peeled off by the guide roller 600 as a winding means is performed. Here, the rotational speed of the winding means in the winding step (S14), the guide roller 600 in the peeling step (S13) and the mesh type cathode drum 200 in the cathode drum rotating step (S12) are the same. It is controlled to be maintained, it is adjusted so that the tension or compression force is applied to the metal mesh (M) wound on the winding means is not broken or stretched phenomenon.

The action of the continuous metal mesh production apparatus by the mesh-type rotary cathode drum plating method and the surface shape of the nickel mesh in the metal mesh plated by the metal mesh production method are illustrated in FIGS. 5A and 5B.

According to this, the shape of the bottom surface (b of FIG. 5) contacting the mesh 242 on the surface of the mesh type cathode drum 200 is formed with a hexagon having a thickness of 30 μm, while the top surface (a of FIG. 5) is formed. The shape forms a hexagon having a thickness of 30 μm and the distance between the hole and the hole is 80 μm. Therefore, it is possible to manufacture a wide and long nickel mesh.

The scope of the present invention is not limited to the above-exemplified embodiments, and many other modifications based on the present invention may be made by those skilled in the art within the above technical scope.

As described in detail above, in the continuous metal mesh production apparatus and manufacturing method according to the present invention, the mesh-type rotary cathode drum plating method includes a mesh-type cathode drum and an insoluble anode in which the surface is directly processed into a mesh form or the mesh is attached to the surface. An anode basket and the like are provided, and the electrolyte is agitated by the electrolyte sprayed while the mesh cathode drum and the anode basket are maintained at a constant distance, and the mesh cathode cathode is rotated so that the metal is plated on the surface thereof.

Therefore, the electrolytic solution is agitated by the electrolytic solution to be sprayed, not only to form a uniform plating layer on the surface of the mesh type cathode drum, but also to produce a large-scale, long-length high-quality metal mesh.

In addition, the rotating mesh-type cathode drum is mounted on the support of the electrolytic cell so that it can be easily detached and maintained, so that the maintenance of the mesh-type cathode drum is easy and the metal cluster is provided in the anode basket so that the mesh-type cathode drum and the anode basket As the distance is kept constant, the effect of preventing the phenomenon in which the positive electrode plate is dissolved in the electrolyte and the shorter the distance between the poles with the progress of electrodeposition is expected.

In addition, the process simplification is expected due to the simplified equipment of the manufacturing apparatus.

Claims (7)

An electrolytic cell in which an electrolyte is accommodated; A mesh type negative electrode drum installed to be partially immersed in the electrolytic solution of the electrolytic cell and rotating with an applied power source; An anode basket installed to be completely immersed in the electrolyte of the electrolytic cell, the anode basket being formed in a shape corresponding to the mesh type cathode drum and maintaining a predetermined distance; An auxiliary tank formed at a lower portion of the electrolytic cell to receive an electrolyte flowing from the electrolytic cell; An electrolytic solution spraying means installed at one side of the electrolytic cell and spraying the electrolytic solution so that the electrolytic solution of the electrolytic cell is stirred; Circulation-filtering means provided on one side of the auxiliary tank to remove foreign substances in the electrolyte while circulating the electrolyte in the auxiliary tank to the electrolytic cell; Winding means provided on one side of the mesh type cathode drum and winding a metal mesh formed on a surface of the mesh type cathode drum; Apparatus for producing a continuous metal mesh by the mesh-type rotary cathode drum plating method, characterized in that provided on one side of the mesh-type cathode drum, the cleaning means for cleaning the surface of the mesh-type cathode drum. The method of claim 1, wherein the mesh-type negative electrode drum can be used by directly processing the surface of the mesh in the form of a mesh or by attaching a mesh (mesh) processed in a weaving type or batch type to the surface. Continuous metal mesh production apparatus by the mesh-type rotary cathode drum plating method. 3. The apparatus of claim 2, wherein the mesh on the surface of the mesh type cathode drum is made of a single metal or an alloy. The apparatus of claim 1, wherein the anode basket is made of an insoluble anode. The method of claim 1 or 4, wherein the anode basket, A drum accommodating portion formed in an arc shape cut in half and accommodating the mesh type cathode drum; A cluster accommodating part formed at one side of the drum accommodating part and accommodating a metal cluster having the same component as the electrolyte of the electrolytic cell; A separation prevention net formed at an outer side of the cluster accommodating part and preventing separation of the metal cluster; Is formed on both ends of the drum accommodating portion, continuous metal mesh manufacturing apparatus by a mesh-type rotating cathode drum plating method comprising a positive power supply connected to the power applied. 6. The apparatus of claim 5, wherein the anode basket is made of titanium (Ti). An electrolytic solution stirring step of spraying an electrolytic solution with an applied power source, and stirring the electrolytic solution of the electrolytic cell, A cathode drum rotating step of rotating the mesh type cathode drum such that the electrolyte solution stirred in the electrolyte stirring step is continuously plated on the surface of the mesh type cathode drum; A peeling step of peeling the metal mesh plated on the surface of the mesh type cathode drum while the cathode drum rotating step is performed; Method for producing a continuous metal mesh by the mesh-type rotary cathode drum plating method comprising a winding step of winding the metal mesh to be peeled off in the peeling step.

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