KR20220135176A - Method of treating waste battery reuse - Google Patents

Abstract

The present invention relates to a processing method for recycling a waste battery. The processing method for recycling a waste battery comprises the steps of: cooling a battery pack including a battery, containing a plurality of lithium ions, as a unit battery for a minimum cooling time or longer which satisfies equation 1, minimum cooling time = A × (W^0.33)(A = 4 × e^(-0.02×dT); and shredding the cooled battery pack, wherein W = battery pack weight (Kg), dT= │external cooling temperature - target temperature│, ││ means the absolute value. According to the present invention, it is possible to treat a waste battery, when shredding the same, by a simple process within a short time.

Description

Treatment method for reuse of waste batteries

To a waste battery, and to provide a treatment method for reuse of the waste battery.

Lithium secondary batteries are used in a very wide field from small electronic devices to automobiles, and their use is gradually expanding.

These lithium secondary batteries can no longer be used due to a decrease in the capacity that can be charged after use for as short as 5 years to as long as 10 years, and the problem of disposing of batteries that can no longer be used in countries around the world is a social issue.

A lithium secondary battery generally includes a positive electrode and a negative electrode containing Ni, Co, Mn, etc., along with lithium, and an electrolyte containing a non-aqueous organic solvent, and a fire may occur due to the organic solvent, and also, the positive electrode Li, Ni, Co, Mn, etc. contained in the are expensive elements, so research for recycling them from waste batteries is being actively conducted.

In particular, among the fields in which such lithium secondary batteries are used, the spread of electric vehicles is increasing, and as such electric vehicles require high output, 20V to 20V to which one or more unit cells of 2V to 4V are connected in series/parallel Since one or more 60V battery modules are used in the form of a battery pack ( FIG. 1 ) connected in series, research on recycling Li, Ni, Co, Mn, etc. from such a battery pack is attracting attention. .

In order to recycle the lithium secondary battery, it is necessary to disassemble the battery, and there is a problem that the battery disassembly, ie, destruction, of the pack unit and the module unit causes a fire. Accordingly, in order to prevent this, as shown in FIG. 2, after the battery is electrically discharged, the battery pack is physically disassembled into a module and a lower unit of the cell, and after complete discharge in brine, firing, crushing and The battery is disassembled by performing specific gravity separation to obtain black powder, which is a mixture of positive electrode material and negative electrode material powder. However, this method has a problem of environmental pollution as hydrogen ions of the electrolyte solvent and ions of the electrolyte salt, for example, fluorine ions combine to generate hydrogen fluoride (HF), a harmful gas during salt water discharge, and after salt water discharge, Wastewater containing chlorine ions emitted can also cause water pollution.

In addition, in this process, in the case of a pack battery, electrical discharge takes 8 hours per pack, on average 1 to 2 hours for physical decomposition, about 24 hours for salt discharge, and about 1 hour for crushing and specific gravity screening process There is a problem that the entire process takes too long as it takes, so it is not suitable for practical application.

Accordingly, there is a need for a method for more easily disassembling a battery, particularly a battery pack in a pack unit.

According to an embodiment of the present invention, a treatment method for reuse of waste batteries is to provide a treatment method for reuse of waste batteries capable of stably crushing a battery pack in a simple process without explosion and fire.

According to one embodiment of the present invention, a battery processing method includes the steps of cooling and freezing a battery pack including a battery including a plurality of lithium ions as unit cells for at least a minimum cooling time satisfying Equation 1 below, and It may include crushing the battery pack.

<Equation 1>

Minimum cooling time = A × (W ^0.33 )

(A = 4 × e ^{(-0.02 × dT)} , W = Battery weight (Kg), dT = │External cooling temperature - Target temperature│, ││ means absolute values)

In one embodiment, the freezing step may be carried out by cooling to -150 ℃ to -60 ℃. In one embodiment, the freezing step is carried out by cooling to -60 °C to -20 °C, and the crushing step may be carried out under conditions of supplying inert gas, carbon dioxide, nitrogen, water, or a combination thereof. .

In one embodiment, the freezing step is carried out by cooling to -60 ℃ to -20 ℃, the crushing step may be carried out under vacuum atmosphere conditions of 100 torr or less. In one embodiment, the crushing may be carried out until the maximum size of the crushed product is 10 mm or less.

In one embodiment, after the crushing step, it may be carried out further comprising the step of magnetic separation or specific gravity screening to separate the product having a maximum size of 1 mm or less. In one embodiment, after the freezing step, before the crushing step, the step of compressing the frozen battery pack may be further included. In one embodiment, the compressing process may be performed to a thickness of 1/2 or less of the thickness of the battery pack before freezing.

According to another embodiment of the present invention, in a battery processing method, a battery pack including a battery including a plurality of lithium ions as a unit cell is cooled and frozen for at least a minimum cooling time satisfying the following Equation 1, and the battery pack is cooled It may include the step of crushing.

<Equation 1>

Minimum cooling time = A × (W ^0.33 )

(A = 4 × e ^{(-0.02 × dT)} , W = Battery weight (Kg), dT = │External cooling temperature - Target temperature│, ││ means absolute values)

In one embodiment, the freezing step may be carried out by cooling to -150 ℃ to -60 ℃. In one embodiment, the freezing step is carried out by cooling to -60 °C to -20 °C, and the crushing step may be carried out under conditions of supplying inert gas, carbon dioxide, nitrogen, water, or a combination thereof. .

In one embodiment, the freezing step is carried out by cooling to -60 ℃ to -20 ℃, the crushing step may be carried out under vacuum atmosphere conditions of 100 torr or less.

In one embodiment, the crushing may be carried out until the maximum size of the crushed product is 10 mm or less. In one embodiment, after the crushing step, it may be carried out further comprising the step of magnetic separation or specific gravity screening to separate the product having a maximum size of 1 mm or less.

According to an embodiment of the present invention, a treatment method for reuse of a waste battery is a simple process without risk of explosion and fire when the battery is crushed through the relationship of the minimum holding time in the refrigerator according to the weight of the battery, and in a short time, can be processed.

1 is a schematic diagram schematically illustrating the structure of a unit cell, a module, and a battery pack;
Figure 2 is a process diagram schematically showing a treatment process of a conventional waste battery.
Figure 3 is a schematic diagram schematically showing a processing method for reuse of a waste battery according to an embodiment.
4 is a graph of voltage change according to the freezing process of the battery pack frozen according to Example 1. FIG.
5 is a photograph of the product crushed according to Example 1.
6 is a photograph of ignition during the crushing process of Comparative Example 1.
7 is a graph of a minimum cooling time, according to an embodiment of the present invention.
8A and 8B are photographs of an Example according to the minimum cooling time of the present invention, and FIGS. 8C and 8D are photographs of a Comparative Example according to the minimum cooling time of the present invention.

The terms first, second, third, etc. are used to describe, but are not limited to, various parts, components, regions, layers and/or sections. These terms are used only to distinguish one part, component, region, layer or section from another part, component, region, layer or section. Accordingly, a first part, component, region, layer or section described below may be referred to as a second part, component, region, layer or section without departing from the scope of the present invention.

The terminology used herein is for the purpose of referring to specific embodiments only, and is not intended to limit the invention. As used herein, the singular forms also include the plural forms unless the phrases clearly indicate the opposite. As used herein, the meaning of "comprising" specifies a particular characteristic, region, integer, step, operation, element and/or component, and the presence or absence of another characteristic, region, integer, step, operation, element and/or component. It does not exclude additions.

When a part is referred to as being “on” or “on” another part, it may be directly on or on the other part, or the other part may be involved in between. In contrast, when a part refers to being "directly above" another part, the other part is not interposed therebetween.

Although not defined otherwise, all terms including technical and scientific terms used herein have the same meaning as commonly understood by those of ordinary skill in the art to which the present invention belongs. Commonly used terms defined in the dictionary are additionally interpreted as having a meaning consistent with the related art literature and the presently disclosed content, and unless defined, are not interpreted in an ideal or very formal meaning.

Hereinafter, embodiments of the present invention will be described in detail. However, this is provided as an example, and the present invention is not limited thereto, and the present invention is only defined by the scope of the claims to be described later.

A treatment method for reuse of waste batteries according to an embodiment comprises the steps of cooling and freezing a battery pack including a battery including a plurality of lithium ions as unit cells for at least a minimum cooling time, and crushing the frozen battery pack. includes steps. The battery containing lithium ions may include various types of batteries containing lithium ions, for example, a lithium secondary battery separated from a vehicle, a secondary battery separated from an electronic device such as a mobile phone, a camera, and a notebook computer. It may be a battery, specifically, a lithium secondary battery.

In the treatment method for recycling waste batteries, in the step of cooling and freezing a battery pack including a plurality of lithium ions as unit cells for a minimum cooling time or more, the minimum cooling time may satisfy Equation 1 below, The battery pack may be frozen by cooling to a value greater than or equal to the value of Equation 1 below.

<Equation 1>

Minimum cooling time = A × (W ^0.33 )

(A = 4 × e ^{(-0.02 × dT)} , W = Battery pack weight (Kg), dT = │External cooling temperature - Target temperature│, ││ means absolute values)

The minimum cooling time of Equation 1 is the battery pack weight, specifically the weight of the battery, the external cooling temperature that is the cooling temperature applied to the battery pack for cooling the battery pack, and the battery pack, specifically the electrolyte solution in the battery pack It means the target temperature for cooling to In the freezing of the battery pack, by performing more than the minimum cooling time, the electrolyte solution inside the battery pack is cooled to stably perform a subsequent process. In the freezing of the battery pack, if the battery pack is frozen for a time less than the minimum cooling time, the electrolyte is not cooled, so that there is a problem that a fire risk may occur when crushed.

According to one embodiment, the freezing process may be carried out at a temperature sufficient for the electrolyte to be frozen, for example, it may be carried out by cooling to -150°C (−150°C) to -60°C (−60°C). . When the battery pack is cooled to the above temperature range, the voltage that is usually minutely remaining inside the battery, for example, about 2V to 3V, is lowered to close to 0V, as shown in FIG. 2, whereby the positive and negative electrodes are directly Since no cell reaction occurs even when a short circuit in contact occurs, the cell temperature does not increase, so that gas generation and combustion of the electrolyte do not occur. In addition, since the electrolyte is in a frozen state, the mobility of lithium ions is very low, and the conduction characteristics according to the movement of lithium ions may be significantly reduced, and since vaporization of the electrolyte does not occur, combustible gases such as ethylene, propylene, hydrogen, etc. may not occur.

When the refrigeration process is out of the above temperature range, for example, when cooling to a temperature higher than -60°C, the voltage remaining inside the battery does not decrease to 0V, and a battery reaction may occur due to a short circuit. , the electrolyte is not completely frozen, which is not appropriate. In addition, when cooling to -150°C, the electrolyte is sufficiently frozen and the internal voltage of the battery is also reduced to 0V, so it is not necessary to lower the temperature to a lower temperature than this.

In another embodiment, the freezing process may be carried out by cooling to a temperature capable of suppressing vaporization of the electrolyte, for example, -60 °C (-60 °C) to -20 °C (-20 °C).

When the freezing process is carried out by cooling to -60 °C (-60 °C) to -20 °C (-20 °C), the condition of supplying inert gas, carbon dioxide, nitrogen, water, or a combination thereof to the crushing process Alternatively, it may be carried out under vacuum atmosphere conditions of 100 torr or less.

The inert gas may be argon gas, helium gas, or a mixture thereof. The pressure of the vacuum atmosphere may be 100 torr or less, 0.00001 (10 ^-5 ) torr to 100 torr.

As such, even when the freezing process is performed at a rather high temperature, such as -60°C to -20°C, the crushing process is performed by supplying an inert gas, carbon dioxide, nitrogen, water, or a combination thereof, or in a vacuum atmosphere with a pressure of 100 torr or less. By controlling the oxygen supply, it is possible to prevent the electrolyte from reacting with oxygen, thereby preventing an explosion, and suppressing the vaporization of the electrolyte, such as ethylene, propylene, hydrogen, etc. It may not generate flammable gas.

When the freezing process is carried out at -60 ° C to -20 ° C, when carried out in an air atmosphere, or when carried out at a pressure exceeding 100 torr, a voltage may remain in the battery pack, and since the electrolyte is not in a frozen state, Due to the remaining voltage, the electrolyte is vaporized due to sparks generated when a short circuit occurs, and an explosion may occur, which is not appropriate.

As such, the treatment method for reuse of waste batteries includes the step of freezing, before crushing the battery pack including the battery such as a lithium secondary battery, safety from the risk of fire that may occur in the process of shredding the battery pack. can be obtained

The crushing of the frozen battery pack may refer to a process of applying impact or pressure to the battery pack so that a portion of the battery pack is separated from the battery pack. The crushing of the frozen battery pack according to an exemplary embodiment may refer to a process of pulverizing the battery pack, a cutting process, a compression process, and combinations thereof. Specifically, the crushing process may refer to any process in which a battery pack is destroyed and a small size can be obtained.

The crushing of the frozen battery pack according to an embodiment may include both compressing the frozen battery pack or destroying the frozen battery pack by applying an external force such as shear force or tensile force. For example, the crushing may be performed using a crusher.

As described above, the processing method according to one embodiment does not physically disassemble the battery pack into modules and unit cells, but rather crushes the battery pack itself, so the process is simple, and by freezing a large amount of batteries at once in the freezing process , it is possible to process and recycle waste batteries within a short period of time. In addition, even in the case of an electric vehicle using a battery pack as an energy source, the processing method according to an embodiment can be applied by separating the battery pack from the vehicle in the form of a battery pack, so that the battery pack can be safely treated with a simple process.

In general, when the battery pack is directly crushed, an explosion and fire may occur due to the electrolyte contained therein. In particular, when a certain pressure is applied to the battery pack, the separator is physically crushed, and a high current is formed due to the occurrence of a short circuit, resulting in a spark. is generated, and the spark may ignite the electrolyte and cause a fire.

In one embodiment, since the battery pack is frozen to suppress ignition of the liquid electrolyte contained in the battery pack, and then the crushing process is performed, there is no problem due to ignition of the electrolyte.

This crushing process may be carried out until the maximum size of the crushed product is 10 mm or less, for example, 0.1 mm to 10 mm. When the crushing process is performed under this condition, a separation process such as magnetic separation or specific gravity separation of crushed products can be effectively applied, and finally the positive electrode material and the positive electrode material of the positive electrode current collector, the negative electrode active material and the negative current collector A powder in which the entire anode material is mixed, for example, black powder can be more easily obtained. In addition, when the crushing process is performed under this condition, the electrolytic solution can be more easily removed from the crushed product.

The crushing process may be performed at least once. Specifically, the crushing process may be continuously or discontinuously performed at least once or more.

Since the crushed product is at room temperature, the electrolyte is also changed to a liquid phase as the temperature increases, that is, the anode and cathode materials contained in the crushed product from the moment of crushing are in an equilibrium state so that a short circuit does not occur. , and when the electrolyte temperature becomes room temperature, the crushed product can be stabilized.

In one embodiment, after the freezing step, before the crushing step, a process of compressing the frozen battery pack may be further performed. This crimping process can be performed so that it may become 1/2 or less of the thickness of the battery pack before freezing, for example, 1/50 - 1/2 thickness. When further performing a crimping|compression-bonding process, a crushing process can be implemented more uniformly. For example, it can be constantly supplied without deviation into the crusher used during the crushing process.

When the compression process is performed to have a thickness exceeding 1/2 of the thickness of the battery pack before freezing, it is difficult to form a constant shape, and accordingly, there may be a problem in that the crushing process time is lengthened.

Subsequently, a step of separating a product having a maximum size of 1 mm or less from the crushed product may be further performed. The separating step may be performed by magnetic selection or specific gravity selection, and any screening process well known in the art may be performed. As described above, as the separation step is further performed, a powder in which the positive electrode active material, the negative electrode active material, and the positive current collector and the negative current collector are mixed can be obtained. In addition, in one embodiment, after performing the crushing process, a process of removing and separating the electrolyte may be performed. In the electrolytic solution removal process, the crushed product may be removed by heat treatment or vacuum drying.

In the treatment method according to another embodiment, the freezing and crushing processes may be performed together. Specifically, the processing method may include crushing the battery pack while freezing the battery pack including the batteries including a plurality of lithium ions as unit cells. In this case, in the freezing step, the frozen state may be maintained for at least the minimum cooling time satisfying Equation 1, and then, the frozen state may be continuously maintained and the crushing process may be simultaneously performed.

<Equation 1>

Minimum cooling time = A × (W ^0.33 )

(A = 4 × e ^{(-0.02 × dT)} , W = Battery pack weight (Kg), dT = │External cooling temperature - Target temperature│, ││ means absolute values)

By performing the freezing and crushing processes at the same time, the process steps may be simplified, and economic advantages may be secured.

In one embodiment, the freezing step may be carried out by cooling to -150 °C to -60 °C. In addition, in the treatment method, the crushing process may be performed under conditions of supplying an inert gas, carbon dioxide, nitrogen, water, or a combination thereof while freezing the battery pack at -60°C to -20°C, and the battery pack While freezing at -60°C to -20°C, the crushing process may be performed under vacuum atmosphere conditions of 100 torr or less. Detailed descriptions thereof are the same as those described above to the extent that they are not contradictory.

In one embodiment, after the step of crushing while freezing, it may be carried out further comprising the step of magnetic screening or specific gravity screening for separating products having a maximum size of 1 mm or less. For the contents of the freezing and crushing process, reference may be made to the above contents to the extent that is not contradictory.

Hereinafter, Examples and Comparative Examples of the present invention will be described. However, the following examples are only examples of the present invention, and the present invention is not limited thereto.

<Example 1>

LiNi _0.6 Co _0.2 Mn _0.2 O ₂ A battery pack including a unit cell including a positive electrode including a positive electrode active material, a negative electrode including an artificial graphite negative active material, and an electrolyte solution was frozen at -80°C. As the electrolyte, a mixed solvent of dimethyl carbonate in which 1.0M LiPF ₆ was dissolved and diethyl carbonate (50:50 volume ratio) was used.

The result of measuring the battery voltage while freezing the battery pack at -80°C is shown in FIG. 4 . As shown in FIG. 4 , since the battery pack exhibits almost the same voltage at a high temperature of about 40°C, room temperature, and -60°C, it can be seen that the battery characteristics are not lost. Subsequently, when the temperature is lowered from -60°C to -70°C, the voltage is rapidly lowered, resulting in the voltage being zero below -70°C, so that the battery pack is stored at -60°C to -150°C. It can be seen that if frozen in a furnace, a short circuit will not occur.

The frozen battery pack was crushed using a shear crusher. This crushing process was performed so that the maximum size of the crushed product was 10 mm or less. A photograph of the crushed product is shown in FIG. 5 .

The crushed product was subjected to specific gravity screening to obtain a product having a maximum size of 1 mm or less.

<Comparative Example 1>

The battery pack used in Example 1 was crushed using the same crusher as in Example 1 without refrigeration. As shown in FIG. 6 in the crushing process, a flame due to a short circuit occurred.

As such, through Example 1 and Comparative Example 1, by including the step of freezing the battery pack including the battery before crushing the battery, in the battery crushing step, a short circuit does not occur and a flame does not occur It can be seen that the stability is excellent.

7 is a graph of a minimum cooling time, according to an embodiment of the present invention.

Referring to FIG. 7 , it can be confirmed that, in the battery processing method according to an embodiment of the present invention, in the step of freezing the battery pack, a minimum cooling time for cooling the battery can be derived. Specifically, it may be confirmed that the minimum cooling time is related to the weight of the battery, the external cooling temperature, and the target temperature.

7 shows the external cooling temperature when the target temperature is set to -70 °C, and the battery weight is 2.5 kg(A), 10 kg(B), 20 kg(C), and 50 kg(D), respectively. and minimum cooling time. When cooling the battery, after a predetermined period of time, the electrolyte of the battery starts cooling and it can be confirmed that the voltage becomes 0. Through this, in cooling the battery, it can be confirmed that the minimum holding time is required to sufficiently cool the inside, specifically, the electrolyte.

Specifically, in a heat transfer situation for cooling in which heat is taken to the outside, when the specific heat of the battery itself is considered, it can be confirmed that the weight of the battery and time for cooling are required. Considering the specific heat of the battery itself, even in a heat transfer situation for cooling where heat is lost to the outside, it can be confirmed that the weight of the battery and time for cooling are required.

As described above, in the present invention, the minimum time required for cooling can be confirmed by using the external cooling temperature for refrigeration, the target temperature, and the weight of the battery in order to cool the battery.

Table 1 below lists the minimum cooling time according to the battery weight and external cooling temperature.

Battery weight [Kg] Out
Cooling
temperature
[℃] target
temperature
[℃] Equation 1 Ieast
Cooling
hour
[h] A_1 2.5 -120 -70 1.9 1.9 A_2 2.5 -100 -70 2.9 2.9 A_3 2.5 -80 -70 4.4 4.4 B_1 10 -120 -70 3.1 3.1 B_2 10 -100 -70 4.6 4.6 B_3 10 -80 -70 7.0 7.0 C_1 20 -120 -70 3.9 3.9 C_2 20 -100 -70 5.8 5.8 C_3 20 -80 -70 8.8 8.8 D_1 50 -120 -70 5.3 5.3 D_2 50 -100 -70 7.9 7.9 D_3 50 -80 -70 11.9 11.9

Referring to Table 1, it can be seen that the smaller the battery weight, the shorter the minimum cooling time of the battery to be cooled is. In addition, when the value of Equation 1 derived from the relational expression according to the battery weight, the external cooling temperature, and the target temperature is cooled with the minimum cooling time, it can be confirmed that the battery, specifically, the electrolyte of the battery is cooled. In addition, when the battery is cooled for a period of time equal to or greater than the value of Equation 1, a fire does not occur in the subsequent process of crushing the battery.

8A and 8B are photographs of an Example according to the minimum cooling time of the present invention, and FIGS. 8C and 8D are photographs of a Comparative Example according to the minimum cooling time of the present invention.

Referring to FIGS. 8A and 8B , in cooling the battery, a fire occurrence state of the crushed material when frozen for less than the required minimum cooling time was tested. In the above experiment, when the battery weight was 25 kg, the external cooling temperature - 95 ° C, and the target freezing temperature - 70 ° C, the value of Equation 1 below was 7 hours, the experiment was carried out for 5 hours lower than the value of Equation 1 .

<Equation 1>

Minimum cooling time = A × (W ^0.33 )

(A = 4 × e ^{(-0.02 × dT)} , W = Battery pack weight (Kg), dT = │External cooling temperature - Target temperature│, ││ means absolute values)

Referring to Figures 8c and 8d, when the battery is frozen for more than the minimum freezing time required for cooling, the fire occurrence state of the crushed material is an experiment. In the above experiment, the same battery weight, external cooling temperature, and minimum freezing time as those of FIGS. 8A and 8B were conducted for 7 hours or more.

Table 2 below compares the fire occurrence states of Examples and Comparative Examples according to the same battery weight, external cooling temperature, and minimum freezing time according to 8a to 8d. The determination of the state of the fire was set to "O" if fire was observed after crushing the battery, and "X" otherwise.

battery weight
[Kg] external cooling
temperature
[℃] target temperature
[℃] Equation 1 real
Cooling time [h] fire Comparative Example 2 25 - 95 - 70 7.0 5 O Example 2 25 - 95 - 70 7.0 7 X

Referring to Table 2, when the battery is cooled to a value smaller than the value of Equation 1 corresponding to the minimum cooling time, the electrolyte is not cooled, and it can be seen that a fire occurs after the battery is crushed. In this way, when the value of Equation 1 is used as the minimum cooling time to cool the battery, it can be confirmed that the crushed material can be stably utilized without fire after the battery is crushed.

The present invention is not limited to the above embodiments, but can be manufactured in a variety of different forms, and those of ordinary skill in the art to which the present invention pertains can take other specific forms without changing the technical spirit or essential features of the present invention. It will be understood that it can be implemented as Therefore, it should be understood that the embodiments described above are illustrative in all respects and not restrictive.

Claims (14)

Cooling a battery pack including a battery including a plurality of lithium ions as unit cells for at least a minimum cooling time satisfying Equation 1 below and freezing; and
and crushing the frozen battery pack.
<Equation 1>
Minimum cooling time = A × (W ^0.33 )
(A = 4 × e ^{(-0.02 × dT)} , W = Battery pack weight (Kg), dT = │External cooling temperature - Target temperature│, ││ means absolute values)
According to claim 1,
The freezing step is a processing method that is carried out by cooling to -150 ℃ to -60 ℃.
According to claim 1,
The freezing step is carried out by cooling to -60 ℃ to -20 ℃,
The crushing step is performed under conditions of supplying inert gas, carbon dioxide, nitrogen, water, or a combination thereof.
According to claim 1,
The freezing step is carried out by cooling to -60 ℃ to -20 ℃,
The crushing step is a processing method that is carried out under vacuum atmosphere conditions of 100 torr or less.
The method of claim 1,
The crushing step is performed until the maximum size of the crushed product is 10 mm or less.
According to claim 1,
After the crushing step, the treatment method carried out further comprising the step of magnetic separation or specific gravity screening to separate the product having a maximum size of 1 mm or less.
According to claim 1,
After the freezing step, before the crushing step, the processing method carried out further comprising a step of compressing the frozen battery pack.
8. The method of claim 7,
The processing method in which the said crimping|compression-bonding process is implemented so that it may become 1/2 or less of the thickness of the battery pack before the said freezing.
A method for processing a battery comprising: cooling and freezing a battery pack including a battery including a plurality of lithium ions as unit cells for at least a minimum cooling time satisfying Equation 1, and crushing the battery pack.
<Equation 1>
Minimum cooling time = A × (W ^0.33 )
(A = 4 × e ^{(-0.02 × dT)} , W = Battery pack weight (Kg), dT = │External cooling temperature - Target temperature│, ││ means absolute values)
10. The method of claim 9,
The freezing step is a processing method that is carried out by cooling to -150 ℃ to -60 ℃.
10. The method of claim 9,
The freezing step is carried out by cooling to -60 ℃ to -20 ℃,
The crushing step is performed under conditions of supplying inert gas, carbon dioxide, nitrogen, water, or a combination thereof.
10. The method of claim 9,
The freezing step is carried out by cooling to -60 ℃ to -20 ℃,
The crushing step is a processing method that is carried out under vacuum atmosphere conditions of 100 torr or less.
10. The method of claim 9,
The crushing step is performed until the maximum size of the crushed product is 10 mm or less.
10. The method of claim 9,
After the crushing step, the treatment method carried out further comprising the step of magnetic separation or specific gravity screening to separate the product having a maximum size of 1 mm or less.

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