KR101586072B1 - Surface treatment apparatus for lead terminal of secondary battery - Google Patents

Abstract

A surface treating apparatus for a lead terminal for a secondary battery is disclosed in the present invention. The surface treatment apparatus includes a surface treatment device for a lead terminal for a secondary battery, comprising: an unwinder and a re-winder disposed at both ends of the apparatus to continuously supply the base material; And a reaction vessel for holding a source gas to be plasmaized while maintaining a vacuum state for plasma processing, wherein the unwinder, the rewinder, and the plasma processing apparatus interposed therebetween are disposed in a reaction vessel It is accommodated together.
According to the present invention, there is provided a surface treatment apparatus for a lead terminal for improving the bond strength between a lead terminal drawn out to the outside from an electrode assembly and a lead terminal film attached on the lead terminal to perform sealing.

Description

TECHNICAL FIELD [0001] The present invention relates to a surface treatment apparatus for a lead terminal for a secondary battery,

The present invention relates to a surface treatment apparatus for a lead terminal for a secondary battery.

2. Description of the Related Art As technology development and production increase in mobile devices such as mobile phones and notebooks, demand for secondary batteries as energy sources is rapidly increasing. In recent years, research and development have been actively conducted for electric vehicles and hybrid vehicles as alternative energy sources for replacing fossil fuels.

Such a secondary battery includes a lead terminal that is drawn out from an electrode assembly as a power generation element and forms a current path of charge and discharge power. Although the lead terminal is subjected to a phosphate treatment and a chromate treatment, the phosphate treatment is a method mainly used for steel materials. When applied to lead terminals of non-ferrous metals, the adhesion between the lead terminals and the insulating film is weakened after the electrolyte test , And the chromate treatment maintains a certain degree of adhesion even after the electrolyte test, but there is an industrial restriction due to the total amount of chromium (6-mercury chromium is regulated by RoHS, which is an environmental regulation).

One embodiment of the present invention provides a surface treatment apparatus for a lead terminal for a secondary battery for improving the bond strength between a lead terminal drawn out from the electrode assembly to the outside and a lead terminal film attached on the lead terminal to perform sealing .

According to an aspect of the present invention, there is provided a surface treatment apparatus for a lead terminal for a secondary battery,

A surface treatment apparatus for a lead terminal for a secondary battery,

An unwinder and a rewinder disposed at both ends of the apparatus to continuously feed the workpiece;

A plasma processing device for receiving and treating the base material between the unwinder and the rewinder; And

And a reaction vessel for maintaining a vacuum state for the plasma treatment and containing a source gas to be plasmaized,

The unwinder, the rewinder, and the plasma processing apparatus interposed therebetween are accommodated together in the reaction vessel.

For example, the plasma processing apparatus, O _2, H ₂ O, Ar, NH ₃ and N ₂ O 1 or more of, or O _2, H ₂ O, Ar, NH ₃ and N ₂ O at least one of It is possible to perform a vacuum plasma treatment using a mixed gas of an inert gas and an inert gas as a source gas to be plasmaized.

For example, in the vacuum plasma treatment, the treatment pressure can be set to 1 torr or less.

For example, in the vacuum plasma treatment, the treatment time may be set to 60 seconds or less.

For example, the base material may include aluminum, copper, or nickel.

For example, the surface treatment apparatus may further include a lead terminal film feeder accommodated in the reaction vessel, for supplying the lead terminal film onto the plasma-treated base material.

For example, the lead terminal film may include at least one selected from the group consisting of a polyolefin, a polyolefin copolymer, and a modified polyolefin.

For example, the lead terminal film feeding device may include:

And a pair of film unwinders and film rewinders for supplying the transfer film with the lead terminal film temporarily attached thereto in a roll-to-roll manner.

For example, the lead terminal film feeding device may include:

A separator for separating the sheet-like lead terminal film from the transfer film continuously supplied between the film unwinder and the film rewinder; And

And a suction nozzle for attaching and picking up the separated lead terminal film and placing it on the base material.

For example, the surface treatment apparatus may further include a holding device and a gripping device for holding the lead terminal film and the base material, which are accommodated in the reaction container.

For example, each of the attaching device and the light guide device may include a pressing press and a supporting stand disposed to face each other with a conveying path through which the base material is conveyed.

For example, a heating means may be built in the press press.

For example, in the above attaching device, the pressing press is brought into contact with the lead terminal film face to face, so that heating and pressing can be performed at the same time.

For example, in the above-mentioned touching device, the pressing press is brought into contact with the base material in a face-to-face manner, so that heating and pressing can be performed at the same time.

For example, a vacuum pump for exhausting the internal gas may be connected to one side of the reaction vessel.

For example, the other side of the reaction vessel may be connected to an introduction pipe for introducing a raw material gas to be plasmaized by the plasma processing apparatus.

According to the present invention, the adhesion strength between the lead terminal and the lead terminal film can be increased by attaching the lead terminal film onto the surface-modified lead terminal through the plasma treatment. Thus, it is possible to prevent deterioration of the electrolyte due to leakage of electrolyte or volatile gas and penetration of foreign matter due to peeling between the lead terminal and the lead terminal film.

In the present invention, by applying a plasma process free from the emission of contaminants such as chromate treatment or phosphate treatment, it can be widely applied to the entire industry without any restriction on the environment.

1 is an exploded perspective view of a secondary battery according to an embodiment of the present invention.
2 is an exploded perspective view of a part of Fig.
3 is a cross-sectional view taken along line III-III in FIG.
4 is an enlarged view of a portion IV in Fig.
5 is a diagram schematically showing a lead terminal processing apparatus according to an embodiment of the present invention.

DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a surface treatment apparatus for lead terminals for a secondary battery according to a preferred embodiment of the present invention will be described with reference to the accompanying drawings. 1 is an exploded perspective view of a secondary battery. Fig. 2 is an exploded perspective view of a part of Fig.

1, the secondary battery includes an electrode assembly 180, electrode tabs 170 extending from the electrode assembly 180, a lead terminal 190 electrically connected to the electrode tabs 170, And a battery case 110 accommodating the electrode assembly 180. [

2, the electrode assembly 180 may be formed by sequentially stacking a first electrode plate 151 and a second electrode plate 152 with the separator 160 interposed therebetween. For example, A stacked structure in which a first electrode plate 151, a separator 160, and a second electrode plate 152 cut in a predetermined size are stacked in this order. In the stacked electrode assembly 180, the battery capacity can be easily increased by increasing the number of stacked electrode plates 150 such as the first electrode plate 151 and the second electrode plate 152. For example, the electrode assembly 180 may be formed by stacking a plurality of first electrode plates 151 and a plurality of second electrode plates 152 to increase the discharge capacity, or to stack the first electrode plates 151 and / The area of the second electrode plate 152 can be enlarged.

However, the electrode assembly 180 is not limited to the stacked structure as illustrated. For example, the electrode assembly 180 may include a separator 160 between the first electrode plate 151 and the second electrode plate 152, It is needless to say that they may be formed in a rolled-up structure wound in a roll form.

The electrode plate 150 may be formed by applying an active material to the surface of the electrode current collector 150a and may include an electrode current collector 150a and an active material layer 150c formed on at least one surface of the electrode current collector 1150a . For example, the first and second electrode plates 151 and 152 may be formed of a positive electrode plate and a negative electrode plate, respectively. In this case, the first electrode plate 151 may be formed on at least one surface of the positive electrode collector and the positive electrode collector. And the second electrode plate 152 includes a negative electrode collector and a negative electrode active material layer formed on at least one surface of the negative electrode collector.

An uncoated portion 150b having no active material layer 150c may be formed at the edge of the electrode plate 150. The electrode tabs 170 may be electrically connected to the uncoated portion 150b and first electrode tabs 171 may be formed on the first electrode tabs 151 and the second electrode tabs 152 through the non- And the second electrode tab 172 may be electrically connected. For example, the connection of the electrode tabs 170 to the non-coated portion 150b may be achieved by resistance welding, ultrasonic welding, laser welding, or the like.

The first and second electrode tabs 171 and 172 may be formed of a positive electrode tab and a negative electrode tab, respectively. The first electrode tab 171 and the second electrode tab 172 may be formed of a metal material having a high conductivity. The first electrode tab 171 may be formed of a metal material such as aluminum or nickel, and the second electrode tab 172 may be formed of a metal material such as copper or nickel.

1, the electrode tabs 170 drawn out from the respective electrode plates 150 laminated to each other are overlapped with each other, and the electrode tabs 170 in a denser form are electrically connected to the lead terminals 190 Lt; / RTI > The lead terminal 190 integrally extended with the electrode tab 170 and the joint portion can be drawn out of the battery case 110. [ For example, the electrode tab 170 and the lead terminal 190 may be bound together by ultrasonic welding or the like.

The lead terminal 190 includes a first lead terminal 191 extending from the first electrode tab 171 and a group of second electrode tabs 172 forming a coupling portion with a group of first electrode tabs 171, And a second lead terminal 192 forming a coupling portion and extending from the second electrode tab 172. For example, the first and second lead terminals 191 and 192 may be formed of the same metal material as the first and second electrode tabs 171 and 172, and may be formed of a metal material such as aluminum, copper, or nickel . Hereinafter, the lead terminal 190 may collectively refer to the first and second lead terminals 191 and 192, or may refer to any one of the first and second lead terminals 191 and 192. The lead terminal 190 is electrically connected to the electrode assembly 180 and can be drawn out of the battery case 110.

The battery case 110 provides an accommodation space S for accommodating the electrode assembly 180 and functions to insulate and protect the electrode assembly 110 from the external environment. The battery case 110 may include first and second cases 111 and 112 forming an accommodation space S for accommodating the electrode assembly 180. The battery case 110 may include first and second cases 111 and 112, By bonding the two cases 111 and 112 to face each other, the electrode assembly 180 can be sealed. More specifically, the inner electrode assembly 180 and the electrolyte (not shown) can be sealed through thermal fusion of the facing sealing portions 111a and 112a of the first and second cases 111 and 112. The battery case 110 may seal the electrode assembly 180 and the electrolyte (not shown) such that at least a part of the lead terminal 190 is exposed.

As shown in FIG. 4, the battery case 110 may include a covering material formed by laminating resin sheets 116 and 117 on both sides of the metal foil 115, and may include, for example, an aluminum laminated sheet. More specifically, the battery case 110 may include a metal foil 115 and may have a laminate structure in which insulating layers 116 and 117 are formed on the inner and outer sides of the metal foil 115. For example, the metal foil 115 may be formed of a metal material such as aluminum or copper having excellent moldability. These metal materials can provide barrier properties to the gas.

First and second insulating layers 116 and 117 may be formed on the inner side and the outer side of the metal foil 115, respectively. For example, the first and second insulating layers 116 and 117 are formed to firmly surround and protect the metal foil 115 so that the metal foil 115 is not exposed to the outside despite the high temperature operating environment and external moisture and impacts. I can do it. For example, the first and second insulating layers 116 and 117 may be formed of a polyethylene terephthalate (PET) film or a nylon film having low hygroscopicity, excellent heat resistance, and sufficient strength and flexibility in folding.

For example, a nylon film excellent in adhesion and penetration strength is used as the first insulating layer 116, and a polyethylene terephthalate film having excellent hygroscopicity is used as the second insulating layer 117, 1 and the second insulating layers 116 and 117 may be formed of different kinds of materials depending on required characteristics. An adhesive layer 119 may be formed between the metal foil 115 and the first and second insulating layers 116 and 117 to mediate coupling between the metal foil 115 and the first and second insulating layers 116 and 117.

A heat-sealable layer 118 may be formed on the innermost side of the battery case 110. The heat-sealable layer 118 is disposed so as to overlap between the first and second cases 111 and 112 and is thermally fused to each other to form the sealing portions 111a and 112a of the battery case 110. [ The heat-sealable layer 118 preferably has a high adhesive strength to each other for mutual coupling between the first and second cases 111 and 112.

The lead terminals 190 drawn out from the electrode assembly 180 accommodated in the battery case 110 can be drawn out through the sealing portions 111a and 112a. At this time, it is preferable that the heat-sealable layer 118 formed on the innermost side of the battery case 110 has a high adhesive strength to the lead terminal film 193 formed on the lead terminal 190.

The heat-sealable layer 118 preferably has a high adhesive strength to each other for mutual coupling between the first and second cases 111 and 112, and particularly has a high adhesive strength to the lead terminal film 193. This prevents the peeling between the first and second cases 111 and 112 and the peeling between the first case 111 and the lead terminal film 193 or the peeling between the second case 112 and the lead terminal film 193 , To prevent leakage of electrolyte and penetration of foreign matter.

For example, the heat-sealable layer 118 may be formed of the same material having excellent affinity with the lead terminal film 193. Adhesion between homogeneous materials is advantageous in terms of adhesive strength because of their excellent affinity to each other. For example, the heat-sealable layer 118 may be formed of a polyolefin such as polypropylene or polyethylene.

The lead terminal 190 extends from the electrode assembly 180 and extends to the outside of the battery case 110 across the sealing portion of the battery case 110. At this time, the lead terminal 190 is insulated from the battery case 110 and can be drawn out to the outside while intersecting the battery case 110. A lead terminal film 193 for sealing between the battery case 110 and the lead terminal 190 may be interposed therebetween.

The lead terminal film 193 may be formed on the lead terminal 190 and may be formed at an intersection of the lead terminal 190 and the battery case 110 along the extending direction of the lead terminal 190. The lead terminal 190 and the battery case 110 come into contact with each other via the lead terminal film 193 at the intersection between the lead terminal 190 and the battery case 110. [

The lead terminal film 193 can function to seal the battery case 110 by bringing the lead terminal 190 and the battery case 110 into close contact with each other. For example, the lead terminal film 193 can be sealed between the lead terminal 190 and the battery case 110 by thermal fusion, thereby preventing leakage of the electrolyte contained in the battery case 110 , And can perform a sealing function for blocking the penetration of external foreign matter.

The lead terminal film 193 is formed on the lead terminal 190 to seal between the lead terminal 190 and the battery case 110. The lead terminal film 193 is required to be adhered on the lead terminal 190 with a high adhesive strength so as not to leak electrolyte inside even in a high temperature operating environment. For example, when the lead terminal film 193 is peeled off from the lead terminal 190, electrolyte or volatile gas leaks to the outside, causing a problem of deterioration of the electrolyte due to penetration of external foreign matter. Therefore, it is preferable that the lead terminal film 193 maintain proper barrier property even in a corrosive environment due to high temperature operating environment and electrolyte contact. As will be described later, the surface of the lead terminal 190 is surface-modified by a plasma treatment to enhance the bonding strength with the lead terminal film 193.

The lead terminal film 193 shown in FIG. 4 is strongly coupled with the surface-modified electrode leads 190 through the plasma treatment. The surface of the electrode leads 190 is modified to be hydrophilic, The terminal film 193 is strongly bonded to the hydrophilic functional group.

The lead terminal 190 drawn out from the electrode assembly 180 forms a step on the sealing portions 111a and 112a of the battery case 110 and the lead terminal film 193 has a step shape of the lead terminal 190 And may have step coverage that can be hermetically sealed.

The lead terminal film 193 may be adhered on the lead terminal 190 and adhered to surround the lead terminal 190 or attached in both directions from the upper and lower surfaces of the lead terminal 190, To the side of the terminal 190. The first and second cases 111 and 112 are connected to each other through the lead terminals 190 to which the lead terminal film 193 is attached so that the first and second cases 111 and 112 are opposed to each other, The inner electrode assembly 180 can be sealed through the thermal fusion of the electrodes 111a and 112a. At this time, the lead terminal film 193 can form a fusion bonding with the innermost heat-sealable layer 118 of the battery case 110, whereby the sealing between the lead terminal film 193 and the electric case 110 Lt; / RTI >

In the present invention, the plasma processing of the lead terminal 190 is included. Here, the plasma treatment is a surface treatment step of modifying the surface of the lead terminal 190 so as to increase the bonding strength between the lead terminal 190 and the lead terminal film 193, thereby imparting an adhesive force to the surface of the lead terminal 190 . Plasma can mean an ionized gas energy state with electrical conductivity, and in general, ions and electrons in the ionized state and neutral particles and active particles can coexist to produce a variety of reactions.

In the present invention, the surface of the lead terminal 190 is surface-modified by vacuum plasma treatment before attachment of the lead terminal film 193, thereby enhancing the surface bonding force. Here, the vacuum plasma treatment is a plasma treatment in a reaction vessel maintaining a vacuum of several tens of Pa or less. More specifically, the plasma treatment is performed by a vacuum plasma treatment using a mixed gas of at least one of O ₂ , H ₂ O, Ar, NH _3, and N ₂ O, or an inert gas thereof as a source gas to be converted into plasma .

For example, an oxide film of Al2O3 is present on the surface of the lead terminal 190 made of an aluminum material. If a plasma discharge is performed using a mixed gas of O ₂ , H ₂ O, Ar, NH _3, and N ₂ O or a mixed gas of these gases with an inert gas, plasma energy is applied to the surface of the lead terminal 190 to form Al 2 O 3 Radicals are generated and O-radicals having strong reactivity react with moisture in the atmosphere or react with reactive O-radicals and H 2 O source gas (or plasma) A hydrophilic functional group such as a hydroxyl group (-OH) is formed on the surface of the lead terminal film 193, and the hydrophilic functional group thus formed reacts with the hydrophilic functional group of the lead terminal film 193 to form a strong bond.

For example, in the plasma treatment using O 2 gas as the source gas, the Al 2 O 3 bond on the surface of the lead terminal 190 is broken by the plasma energy, and O-radicals are present on the surface of the lead terminal 190. When air is injected into the reaction vessel, reactive O-radicals react with moisture to form a hydrophilic functional group such as a hydroxyl group (-OH) on the surface of the lead terminal 190, and the thus formed hydrophilic functional group It reacts with the hydrophilic functional group of the lead terminal film 193 and forms a strong bond.

For example, in the plasma treatment using H2O gas as the source gas, a hydrophilic functional group such as a hydroxyl group (-OH) is formed on the surface of the lead terminal 190 during the vacuum plasma treatment, It reacts with the hydrophilic functional group of the terminal film 193 and forms a strong bond.

A hydrophilic functional group such as a hydroxyl group (-OH) formed on the surface of the lead terminal by the plasma treatment reacts with the hydrophilic functional group on the surface of the lead terminal film 193 and the lead terminal 190 and the lead terminal film 193 are strong Bond.

As described above, when the lead terminal film 193 is formed on the plasma-treated lead terminal 190, the lead terminal film 193 is not easily peeled off. The force by which the lead terminal film 193 is not peeled off from the lead terminal 190 can be expressed by peel strength (N / mm).

Table 1 below shows the results of the internal electrolyte peeling test according to the plasma treatment conditions.

Applied voltage / treatment time 5 seconds 10 seconds 30 seconds 60 seconds 65 W / mm2 Exfoliation Exfoliation Exfoliation Exfoliation 130 W / mm2 Exfoliation 10.8 to 20.2 N / 15 mm 15.4 to 29.1 N / 15 mm 10.2 to 31.5 N / 15 mm 195 W / mm2 20.8 to 29.5 N / 15 mm 29.4 to 39.7 N / 15 mm 36.8 to 55.9 N / 15 mm 22.1 to 51.5 N / 15 mm 260 W / mm2 24.6 to 33.8 N / 15 mm 32.9 to 44.2 N / 15 mm 23.9 to 40.1 N / 15 mm 14.3 to 42.0 N / 15 mm 325 W / mm2 30.1 to 41.8 N / 15 mm 38.2 to 52.9 N / 15 mm Exfoliation Exfoliation 455 W / mm 2 37.1 to 47.8 N / 15 mm 33.5 to 45.5 N / 15 mm Exfoliation Exfoliation

For the peeling test, a lead terminal film 193 was attached on the plasma-treated lead terminal 190, and the substrate was immersed for 24 hours in a high-temperature electrolytic solution of 85 degrees Celsius, and then peel test was performed using a tensile tester .

At this time, the lead terminal film 193 is thermally fused onto the plasma-treated lead terminal 190 by applying a pressure of 0.4 MPa for 3 seconds at a high temperature of 150 ° C. and then applying a pressure of 0.4 MPa The lead terminal film 193 was thermally fused onto the lead terminal by performing pressure application.

Then, both ends of the lead terminals on which the lead terminal film 193 was formed were bonded to a tensile tester, and the tensile strength, that is, the peel strength, was measured while peeling the lead terminal film while increasing the tensile force between both ends. For reference, in the display of the peel strength, "/ 15 mm" indicates that the width of the metal foil is 15 mm.

The lead terminal 190 was subjected to vacuum plasma treatment and O2 gas was used as a source gas to be plasmaized. Under each treatment condition, the applied voltage of the vacuum plasma is represented by the power per unit area (W / mm < 2 >). For each applied voltage, different plasma processing times were applied, and the processing pressure was 50 mtorr.

It can be seen that sufficient peel strength can not be obtained even when the processing time is changed from 5 seconds to 60 seconds when the applied voltage of the vacuum plasma is 65 W / mm 2, and the lead terminal film is directly peeled off without substantial tensile force application. From these results, it is preferable that the applied voltage of the vacuum plasma is larger than at least 65 W / mm 2.

When the applied voltage of the vacuum plasma is 130 W / mm < 2 >, the lead terminal film is peeled off immediately at the processing time of 5 seconds, but it can be endured to some extent at the processing time of 10 seconds or more. It can be seen that when the applied voltage of the vacuum plasma is 195 W / mm 2, it can withstand the tensile force to some extent even at the processing time of 5 seconds. From these results, it is preferable that the applied voltage of the vacuum plasma is at least 130 W / mm 2, more preferably at least 195 W / mm 2.

When the applied voltage of the vacuum plasma is 260 W / mm 2, the lead terminal film 193 can not withstand a certain tensile force at various processing times of 5 to 60 seconds, and the lead terminal film 193 is not immediately peeled off without application of a tensile force. However, when the applied voltage of the vacuum plasma is 325 W / mm < 2 >, it can be seen that the lead terminal film is immediately peeled off without substantially applying a tensile force at a processing time of 30 seconds or more. Similarly, even if the applied voltage of the vacuum plasma is 455 W / mm 2, it can be seen that the lead terminal film is immediately peeled off without substantially applying a tensile force at a processing time of 30 seconds or more. From these results, it is preferred that the applied voltage of the vacuum plasma is at least 325 W / mm 2, more preferably at most 260 W / mm 2. In order to avoid peeling of the lead terminal film immediately without application of a tensile force, the applied voltage of the vacuum plasma is preferably set to 195 W / mm 2 or more and 260 W / mm 2 or less (195 W / mm2 to 260 W / mm2).

When the plasma treatment time is relatively short, for example, in the treatment time of 5 seconds or 10 seconds, the peeling strength tends to increase as the applied voltage is increased. However, when the plasma treatment time is relatively long, At a treatment time of 60 seconds, it is generally found that the peel strength increases as the applied voltage increases, and as the applied voltage increases, the peel strength decreases rather than the appropriate applied voltage. For example, at a processing time of 30 seconds or more, the maximum peel strength is observed at 195 W / mm < 2 >.

In conclusion, considering the applied voltage and the processing time of the vacuum plasma, considering the plasma processing intensity, it is not high that the peeling strength is high because the plasma processing strength is high, and it is desirable to maintain the plasma processing strength at an appropriate level.

The bonding strength between the electrode lead 190 and the lead terminal film 193 is a key to the surface bonding force of the electrode lead 193 and simply increases the plasma processing strength so that the plasma reaction layer is formed thick on the surface of the electrode lead 190 The adhesive strength is not increased. For example, when the applied voltage and the treatment time are set to be excessively higher than the proper level in the plasma treatment using O 2 as the source gas, an oxide film is formed thick on the surface of the electrode lead 190, so that the surface activity, It is. For this reason, the peel strength is not simply increased in proportion to the plasma processing strength, and maintaining the plasma processing strength at an appropriate level can increase the surface bonding force of the lead terminal 190, which is preferable in view of the processing cost and process time.

On the other hand, when the plasma processing time is 30 seconds or more, it can be seen that the lead terminal film 193 is peeled off immediately when the applied voltage is small or large or deviated to one side. That is, when the plasma processing time is 30 seconds or more, when the applied voltage is as small as 65 W / mm < 2 > and when it is increased to 325 W / mm < 2 >, the lead terminal film is peeled without substantial tensile force. It is preferable to limit the plasma processing time to less than 30 seconds, and more preferably to less than 10 seconds in that the increase of the plasma processing time is accompanied by a burden of cost increase and the processing time is delayed.

For example, in order to be able to withstand a certain tensile force at a wide range of applied voltages, the plasma treatment time is preferably greater than 5 seconds but less than 30 seconds, more preferably greater than 5 seconds but less than 10 seconds. For example, when the plasma processing time is 10 seconds, if the applied voltage is larger than 65 W / mm < 2 >, the lead terminal film 193 can be prevented from being immediately peeled off, It is possible to avoid the no-load delamination of the spring 193.

Considering both the applied voltage and the treatment time of the plasma treatment, the maximum peeling strength is obtained at a treatment time of 5 seconds at an applied voltage of 455 W / mm 2, and the maximum peeling strength at an applied voltage of 260 W / mm 2 to 325 W / Strength is obtained. At an applied voltage of 130 W / mm 2 to 195 W / mm 2, the maximum peel strength is obtained at 30 seconds. The reason why the maximum peeling strength is obtained at a relatively short processing time as the applied voltage increases is that the peeling strength in proportion to the plasma processing intensity in terms of the plasma processing intensity, Is not increased, and it is desirable to maintain the plasma processing intensity at an appropriate level.

The results of the experiment for peeling off the electrolyte according to the plasma treatment conditions described above are the results that are obtained when the same raw material gas as the same high frequency power source is used in the plasma processing apparatus having the same structure. Must be different.

Table 2 shows the results of the electrolyte detachment test according to the comparative example in comparison with the present invention.

Immersion time 60 seconds 120 seconds 180 seconds 240 seconds Peel strength 26 to 43 N / 15 mm
37 to 47 N / 15 mm 34 ~ 51N / 15mm
41 to 50 N / 15 mm
37 to 51 N / 15 mm 34 to 49 N / 15 mm
26 to 44 N / 15 mm
31 ~ 40N / 15mm
31 ~ 41N / 15mm
37 to 46 N / 15 mm Uniformity Central unfused fusion discovery Corner unfused N / A Central part, edge not found

In the above comparative example, a chromate film is formed on the surface of the lead terminal by using a chromate treatment solution. More specifically, the lead terminal is immersed in the chromate treatment solution, and after a predetermined time has elapsed, it is dried at 180 degrees for 2 minutes. Then, a lead terminal film was attached on the lead terminal, and the lead terminal film was immersed in the electrolytic solution at 85 ° C for 24 hours, and then the peel test was carried out using a tensile tester.

At this time, the lead terminal film is thermally fused onto the chromated lead terminal. The lead terminal film is thermally fused with a pressure of 0.4 MPa for 3 seconds at a high temperature of 150 ° C. and then subjected to a pressure of 0.4 MPa for 3 seconds at 200 ° C. Whereby the lead terminal film was thermally fused onto the lead terminal.

Then, both ends of the lead terminals having the lead terminal films formed thereon were put on a tensile tester, and tensile strength, i.e., peel strength, was measured when the lead terminal films were peeled while increasing the tensile force between both ends. For reference, in the display of the peel strength, "/ 15 mm" indicates that the width of the metal foil is 15 mm.

As can be seen from Table 2, it can be seen that the peeling strength increases largely as the immersion time of the chromate solution increases. The peel strength of the chromated lead terminal shows a value similar to the peel strength of the plasma-treated lead terminal shown in Table 1. [

However, in the chromate treatment, environmental pollution occurs due to the generation of harmful substances such as hexavalent chromium. Therefore, the product is subject to stringent environmental regulations (RoHS) and has industrial limitations such as the total amount of chromium, A post-processing problem occurs.

In the present invention, by applying the plasma treatment, it is possible to provide an eco-friendly treatment technology in which no polluting gas, wastewater or the like is generated. In other words, phosphate or chromate treatment using heat and chemicals can be considered in the surface treatment process of the lead terminal. However, in this chemical method, environmental problems such as odor and water pollution of floating materials, explosion due to reaction with water Therefore, the present invention uses a physical method, that is, a plasma processing method which is a dry method.

On the other hand, as can be seen from Tables 1 and 2, it can be seen that the plasma treatment time of the present invention takes a remarkably short time compared with the chromate treatment time of the comparative example. The process time can be shortened and high productivity can be expected.

5 is a diagram schematically showing a surface treatment apparatus for a lead terminal for a secondary battery according to an embodiment of the present invention.

The surface treatment apparatus can continuously perform the plasma surface treatment and the attachment of the lead terminal film (f) by receiving the base material (m) of the lead terminal supplied in a roll-to-roll manner. More specifically, the surface treatment apparatus includes an unwinder 451 around which the base material m of the lead terminal is wound, and a base material m of the lead terminal that has been drawn out from the unwinder 451 and has been processed And a pair of rewinders 452 that are rewound in the form of rolls are provided at both ends so as to receive the base material m of the lead terminals continuously supplied between the unwinder 451 and the rewinder 452, Devices for carrying out the attachment of the terminal film (f) are interposed. Between the unwinder 451 and the rewinder 452, a conveying roller 455 or a grounding roller 412 for guiding the base material m of the lead terminal in the traveling direction may be disposed.

The plasma processing apparatus includes a plasma head 411 for generating a high frequency electric field when a high frequency voltage is applied by the high frequency power source 415 and converting the source gas into plasma, and the plasma head 411 and the base material m The surface of the base material m can be treated by the plasma generated between the ground roller 412 that feeds the base material m.

For example, when the plasma is generated by the high frequency electric field between the ground roller 412 and the plasma head 411 providing the ground, the generated plasma causes a predetermined reaction on the surface of the base material m.

When a high frequency voltage is applied from the high frequency power source 415 outside the reaction vessel 401, a high frequency electric field is generated through the plasma head 411 and the high frequency electric field is applied to the reaction vessel 401 ) Is plasmaized, and the generated plasma is ejected onto the surface of the base material (m).

In the surface treatment apparatus of the present invention, the vacuum pump 468 provided on the exhaust pipe 461 connected to the reaction vessel 401 is first operated to reduce the pressure to a vacuum level of several tens of Pa. The raw material gas is introduced into the reaction vessel 401 by opening a control valve (not shown) under the control of, for example, an MFC (mass flow controller) 485, Gas is introduced into the reaction vessel 401. A plasma is generated by applying a high frequency voltage to the plasma processing apparatus 410 and a plasma processing is performed by receiving the base material m continuously transferred between the unwinder 451 and the rewinder 452.

On the other hand, when the surface treatment of the base material m of one roll is completed, the operation of the vacuum pump 468 is stopped and the leak valve 465 is opened to inject air into the reaction vessel 401, (M) of the surface-treated rewinder 452 is pulled out.

The lead terminal film feeder 420 includes a pair of film unwinders 421 and a film rewinder 422 for feeding the feed film temporarily attached with the lead terminal film f in a roll- And a separator (425) for separating the single piece of lead terminal film (f) from the continuously fed film, wherein the lead terminal film (f) separated from the conveying film is attached and picked up, And may include a suction nozzle 428 for seating on the base material m of the terminal. The suction nozzle 428 picks up a single lead terminal film f at the pick-up position and places it on the base material m of the lead terminal. The lead terminal film f seated on the base material m of the lead terminal can be thermally fused onto the base material m of the lead terminal through the later-described adhesion and adherence devices 430 and 440 as described later.

The attaching device 430 may include a pressing press 431 having a heating unit 435 built therein. For example, by providing the heat generating means 435 in the press press 431 for pressing the lead terminal film f onto the base material m of the lead terminal, pressurization and heating can be performed at the same time, By applying the predetermined heat together, the lead terminal film (f) is thermally fused onto the base material (m) of the lead terminal. For example, the lead terminal film (f) may be attached on the base material (m) of the lead terminal in a molten state or a semi-molten state.

The connecting device 430 includes a pressing press 431 and a supporting stand 432 which are disposed to face each other with a conveying path through which the base material m of the lead terminal is conveyed, 431 and the support 432, and intermittently perform the abutment. At this time, the press press 431 contacts the lead terminal film f in a face-to-face manner, and presses the lead terminal film f against the base material m while applying a predetermined heat. For example, in the above step, a pressure of 0.1 to 1.0 MPa is applied at a temperature of 140 to 160 degrees, and as described later, since the temperature is lower than the relative temperature (180 to 240 degrees) There is no problem such that the lead terminal film (f) completely melts and flows down even when the film (f) is directly brought into contact with and heated.

The lead terminal film f may be formed by applying a predetermined heat together with the press pressure to the lead terminal film f, Can be thermally fused onto the base material (m).

The lead-in device 440 includes a press press 441 and a support base 442 which are disposed to face each other with a conveyance path through which the base material m is conveyed. The lead terminal film f is pressed by a press press 441 and the support base 442 and intermittently perform the adherence. At this time, the press press 441 contacts the base material m of the lead terminal in a face-to-face manner, and simultaneously presses the base material m against the lead terminal film f. For example, in the above-mentioned incident, since a pressure of 0.1 to 1.0 MPa is applied at a temperature of 180 to 240 degrees, the lead terminal film (f) having a low melting point is heated to a relatively higher temperature than the temperature Face contact with the base material (m) of the non-lead terminals.

For example, the adhering device 430 and the pointing device 440 may exhibit a difference in specific heating temperature, pressure, and process time. For example, the adhering apparatus 430 may perform bonding for 1 to 10 seconds at a heating temperature of 140 to 160 degrees and a pressure of 0.1 to 1.0 MPa, and the adhering apparatus 440 may be heated at 180 to 240 degrees The bonding can be performed at a temperature of 0.1 to 1.0 MPa for 1 to 10 seconds.

If necessary, the adhesion and the adhesion can be performed twice or more times. For example, a plurality of cycles can be repeatedly performed, with the crosstalk and the adversary being one cycle. In another embodiment of the present invention, as in the case of, for example, four times of folding, four times of folding, four times of folding, Can be performed three times. For example, the adhering device 430 and the touching device 440 can perform bonding with intermittent clearance. Repeating the multiple times of bonding with intermittent clearance is problematic in that, if continuous continuous long-time bonding is performed, the lead terminal film (f) having a low melting point is completely melted to lose the film form and flow down It is because. For similar reasons, the relatively low heating temperature can be performed relatively four times, and the relatively high heating temperature can be performed three times relatively little.

On the other hand, a pair of unwinder 451 and a rewinder 452, a plasma processing device 410 interposed therebetween, a lead terminal film feeder 420, a joining device 430, 440) can be accommodated together in the reaction vessel 401 together. The reaction vessel 401 functions to hold a source gas which is plasmaized by a high voltage electric field which is held between the plasma head 411 and the base material m of the lead terminal while maintaining a vacuum state for the plasma surface treatment . More specifically, a vacuum pump 468 is connected to one side of the reaction vessel 401. The vacuum pump 468 can discharge the internal gas of the reaction vessel 401 through the exhaust pipe 461 and maintain the inside of the reaction vessel 401 at a vacuum level of several tens Pa.

The reaction vessel 401 is connected to an introduction pipe 481 for introducing a raw material gas to be plasmaized by the plasma processing apparatus 410. For example, the raw material gas may be introduced into the reaction vessel 401 through the introduction pipe 481. The introduction pipe 481 may be connected to the gas container 488 containing the raw material gas and the raw material gas in the gas container 488 may be introduced into the reaction vessel 401 at a flow rate controlled by a mass flow controller 485 Can be introduced.

In the surface treatment apparatus of the lead terminal shown in Fig. 5, the base material m of the lead terminal is placed inside the reaction vessel 401 for holding the source gas to be plasmaized while maintaining the vacuum state for the plasma surface treatment, A series of devices 410, 420, 430, and 440 for processing in a two-roll manner are accommodated. Accordingly, it is not necessary to open and close the chamber and control the internal gas or the internal pressure for each step. In addition, since the entire process is performed in a vacuum state, it is possible to fundamentally eliminate the occurrence of defective products due to the inflow of impurities.

While the present invention has been described with reference to exemplary embodiments, it is to be understood that the invention is not limited to the disclosed exemplary embodiments, but, on the contrary, is intended to cover various modifications and equivalent arrangements included within the spirit and scope of the appended claims. Accordingly, the true scope of the present invention should be determined by the technical idea of the appended claims.

110: Battery case 111: First case
111a: sealing part of the first case 112:
112a: sealing part of the second case 115:
116: first insulation layer 117: second insulation layer
118: heat fusion layer 119: adhesive layer
150: electrode plate 150a: electrode current collector
150b: solid portion 150c: active material layer
151: first electrode plate 152: second electrode plate
160: separator 170: electrode tab
171: first electrode tab 172: second electrode tab
180: electrode assembly 190: lead terminal
193: lead terminal film
401: Reaction vessel 410: Plasma processing device
411: Plasma head 412: Ground roller
420: lead terminal film feeder 421: film unwinder
422: film rewinder 425: separator
428: suction nozzle 430: attachment device
431, 441: Pressing presses 432, 442:
435, 445: Heating means 440:
451: Un Winder 452: Rewinder
455: Feed roller 485: MFC
481: introduction pipe of raw material gas 488: gas container
461: Exhaust pipe 465: Leak valve
468: Vacuum pump 415: High frequency power source
S: Capacitance space m: Base material of lead terminal
f: lead terminal film

Claims (16)

A surface treatment apparatus for a lead terminal for a secondary battery,
An unwinder and a rewinder disposed at both ends of the apparatus to continuously feed the workpiece;
A plasma processing device for receiving and treating the base material between the unwinder and the rewinder; And
And a reaction vessel for maintaining a vacuum state for the plasma treatment and containing a source gas to be plasmaized,
The unwinder, the rewinder, and the plasma processing apparatus interposed therebetween are accommodated together in the reaction vessel,
Further comprising a lead terminal film feeder accommodated in the reaction vessel for feeding the lead terminal film onto the plasma-treated base material,
And a joining device and an attracting device for joining the lead terminal film and the base material, the joining device being housed in the reaction container,
Wherein each of the attaching device and the touching device includes a press press and a support stand disposed to face each other with a conveying path through which the base material is conveyed,
In the above-described attaching device, the pressing press is brought into contact with the lead terminal film in a face-to-face manner to simultaneously perform heating and pressing,
In the above-mentioned input device, the pressing press is brought into contact with the base material in a face-to-
Wherein the bonding apparatus performs bonding at a heating temperature of 140 to 160 degrees and the bonding apparatus performs bonding at a heating temperature of 180 to 240 degrees. The method according to claim 1,
The plasma processing apparatus may further comprise at least one of O ₂ , H ₂ O, Ar, NH ₃ and N ₂ O or at least one of O ₂ , H ₂ O, Ar, NH ₃ and N ₂ O, Characterized in that a vacuum plasma treatment is carried out using a mixed gas as a source gas to be plasmaized. 3. The method of claim 2,
Wherein in the vacuum plasma treatment, the processing pressure is not more than 1 torr. 3. The method of claim 2,
Wherein in the vacuum plasma treatment, the treatment time is 60 seconds or less. The method according to claim 1,
Wherein the base material comprises aluminum, copper, or nickel. delete The method according to claim 1,
Wherein the lead terminal film comprises at least one selected from the group consisting of a polyolefin, a polyolefin copolymer and a modified polyolefin. The method according to claim 1,
The lead terminal film feeding device includes:
And a pair of film unwinders and film rewinders for supplying the transfer film temporarily adhering the lead terminal film in a roll-to-roll manner. 9. The method of claim 8,
The lead terminal film feeding device includes:
A separator for separating the sheet-like lead terminal film from the transfer film continuously supplied between the film unwinder and the film rewinder; And
And a suction nozzle for attaching and picking up the separated lead terminal film and placing it on the base material. delete delete The method according to claim 1,
Wherein a heating means is built in the press press. delete delete The method according to claim 1,
And a vacuum pump for exhausting the internal gas is connected to one side of the reaction vessel. The method according to claim 1,
And the introduction pipe of the raw material gas to be plasmaized by the plasma processing apparatus is connected to the other side of the reaction vessel.

Images