JP5708761B2 - Method for removing moisture from lithium ion secondary battery - Google Patents

Description

  The present invention relates to a method for removing moisture from a lithium ion secondary battery.

  In recent years, lithium ion secondary batteries have been known as batteries for portable electronic devices, hybrid electric vehicles, and electric vehicles. Lithium ion secondary batteries have a higher energy density, lighter weight, and higher voltage than other secondary batteries such as nickel metal hydride batteries and nickel cadmium batteries. In the automobile industry in particular, expectations are high as a clean energy source, and various types of lithium ion secondary batteries have been developed.

Typical positive electrode active materials include transition metal oxides such as lithium manganate and lithium cobaltate. For the negative electrode, for example, a carbon-based material is used on the surface of a copper foil. As an electrolytic solution, for example, a lithium salt electrolyte such as lithium hexafluorophosphate (LiPF ₆ ) dissolved in an organic solvent is known.
By the way, when water exists in the electrolyte solution of the lithium ion secondary battery, the residual water in the electrolyte solution reacts with the electrolyte (LiPF ₆ ) to generate hydrofluoric acid (HF). This hydrofluoric acid (HF) affects the SEI (Solid Electrolyte Interface) coating (hereinafter referred to as coating) on the electrode surface to increase resistance, and also reacts with the electrode active material to decrease the battery capacity. Therefore, a manufacturing process is known in which residual water in the electrolytic solution is removed in advance, and an electrolytic solution having a low water content is injected into the battery cell. For example, Patent Document 1 discloses a technique for electrolyzing and removing moisture in an electrolytic solution using a dedicated electrolytic layer.

  However, in this technique, since water contained in the electrolyte before the battery cell injection is electrolyzed, there is a possibility that water is mixed when the electrolyte is injected into the battery cell. In addition, when the electrolytic solution is injected into the battery cell, moisture contained in electrodes, separators, battery cases and the like constituting the battery may be mixed into the electrolytic solution. For this reason, attempts have been made to remove moisture by vacuum drying the electrodes before assembly, but there is a problem that the drying process is costly and is not suitable for the production of small lot batteries.

  Therefore, a technique for removing moisture in the battery cell has also been proposed. For example, Patent Document 2 describes a technique for electrolyzing moisture contained in a battery by applying a voltage after injecting an electrolytic solution into a container.

JP-A-11-233122 JP 2005-56609 A

  However, in the technique described in Patent Document 2, a voltage is applied between electrodes by using an electrode different from a pair of electrodes constituting a container or a power storage element as an electrode for electrolysis. For this reason, it is necessary to add components for electrolysis in the manufacture of the battery, and the material is limited when the container is used as an electrode.

  In addition, as a method of charging a lithium ion secondary battery, constant current charging is performed immediately after the start of charging until the battery voltage is close to the upper limit voltage, and the constant current is decreased while the charging current is reduced from the time when the battery voltage approaches the upper limit voltage. Constant current / constant voltage charging is performed. When performing the first charging in the manufacturing process of the lithium ion secondary battery (hereinafter also referred to as the first charging), when performing the above constant current / constant voltage charging, water electrolysis occurs as the voltage increases, Formation of the negative electrode coating proceeds. For this reason, the reaction for forming the film occurs before the water is sufficiently removed, so that the moisture remaining in the electrolytic solution affects the film formation and further affects the performance of the battery. On the other hand, Patent Document 2 does not consider the effect of such water electrolysis operation on the coating.

  The present invention has been devised in view of such a problem, and a lithium ion secondary battery capable of reducing the manufacturing cost while contributing to further improvement in battery performance relative to a battery having a normal configuration. It is an object of the present invention to provide a method for removing moisture.

In order to achieve the above object, the water removal method for a lithium ion secondary battery of the present invention is a method for removing water contained in a lithium ion secondary battery composed of a positive electrode, a negative electrode, a separator, and an electrolyte solution, The positive electrode current collector is aluminum, the negative electrode current collector is copper, and moisture is removed from the lithium ion secondary battery by applying a voltage to the lithium ion secondary battery. A charge step including a region where charging is performed at a charging voltage that is a voltage equal to or higher than an electrolysis voltage of water and lower than a voltage at which a negative electrode film forming reaction occurs. A discharge step including a region where discharge is performed at a discharge voltage that is lower than the electrolysis voltage of water, and in the moisture removal step, the charge step and the discharge step Was carried out alternately, the then voltage periodically changing the applied to the lithium ion secondary battery, with an increase of the elapsed time from the start of charging, increasing the discharge voltage, the discharge voltage, the current collector of the negative electrode This is characterized in that the voltage is higher than the voltage at which copper is eluted .

  In the charging step, constant current charging is performed at a predetermined current value until the battery voltage reaches the charging voltage, and constant voltage charging is performed at the charging voltage when the battery voltage reaches the charging voltage, In the discharging step, it is preferable that constant current discharge is performed at a predetermined current value until the battery voltage reaches the discharge voltage, and constant voltage discharge is performed at the discharge voltage when the battery voltage reaches the discharge voltage.

  According to the method for removing moisture from a lithium ion secondary battery according to the present invention, by periodically changing the voltage applied to the lithium ion secondary battery in the moisture removing step, the moisture contained in the battery can be efficiently electrolyzed. Can be removed. Thereby, the influence of the water | moisture content on film formation can be reduced, and the performance of a battery can be improved. Moreover, the water | moisture content contained in an electrode can be removed by performing an electrolysis using an electrode.

Further, by alternately repeating the charging step and the discharging step, the gas adhering to the electrode surface in the charging step can be removed in the discharging step, so that the efficiency of moisture removal can be increased.
Further, in this embodiment, by increasing the period of the charging step with the increase in the elapsed time of charging, it becomes possible to perform the reaction by attracting moisture present in the electrolyte more to the electrode, Moreover, it becomes possible to further reduce the gas adhering to the electrode surface, and the efficiency of moisture removal can be enhanced.

Immediately after the start of the first charge, the charge voltage is lowered, moisture removal progresses, and the charge voltage is increased as the moisture in the electrolyte decreases. It becomes possible to do.
Elapsed time after injecting electrolyte, current collector is unlikely to elute, discharge at a low voltage in the initial stage of the initial charging process, and discharge voltage as current collector becomes more likely to elute over time By raising the water content, it is possible to remove moisture with less influence on the elution of the current collector.

  In addition, by performing constant current charging and constant current discharging, it is possible to quickly control the battery voltage value to a target value, and by performing constant voltage charging and constant voltage discharging, moisture removal and gas removal are possible. It is possible to charge and discharge while maintaining a battery voltage suitable for the above.

It is a figure which shows the change of the battery voltage in the manufacturing method of the lithium ion secondary battery which concerns on one Embodiment of this invention. It is a figure which shows the change of the battery voltage in the manufacturing method of the lithium ion secondary battery which concerns on one Embodiment of this invention. It is a figure which shows the change of the battery voltage in the manufacturing method of the lithium ion secondary battery which concerns on one Embodiment of this invention. It is a figure which shows typically the structure of the lithium ion secondary battery which concerns on one Embodiment of this invention. It is a flowchart which shows the outline | summary of the manufacturing method of the lithium ion secondary battery which concerns on one Embodiment of this invention.

Hereinafter, a method for removing moisture from a lithium ion secondary battery according to an embodiment of the present invention will be described with reference to the drawings.
FIG. 1 is a diagram illustrating changes in battery voltage in a water removal step and an initial charging step in a method for manufacturing a lithium ion secondary battery.
FIG. 4 is a diagram schematically showing the configuration of the lithium ion secondary battery.
FIG. 5 is a flowchart showing an outline of a method for manufacturing a lithium ion secondary battery.

  The method of manufacturing a lithium ion secondary battery to which the present invention is applied is a method of assembling a lithium ion secondary battery and charging the assembled lithium ion secondary battery for the first time. Specifically, an assembly process for assembling a lithium ion secondary battery, a moisture removal process for removing moisture inside the lithium ion secondary battery by applying a voltage to the lithium ion secondary battery, and formation of a negative electrode film And an initial charging step for performing charging.

  The method for removing moisture from a lithium ion secondary battery according to the present invention is a method related to the above-described moisture removal step, and removes the moisture inside the lithium ion secondary battery by applying a voltage to the lithium ion secondary battery. Is the method. Here, by periodically changing the voltage applied to the lithium ion secondary battery, moisture in the battery is efficiently removed, and side reactions accompanying charging and discharging are suppressed.

  The method for removing moisture from a lithium ion secondary battery according to the present invention includes a charging step in which water in the battery is electrolyzed by charging the lithium ion secondary battery, and the adsorbed gas of the electrode by discharging from the lithium ion secondary battery. It is preferable to have a discharge step for removing and to alternately perform the charge step and the discharge step.

[1. Battery configuration]
A lithium ion secondary battery manufactured by a method for manufacturing a lithium ion secondary battery to which the present invention is applied will be described.
As shown in FIG. 4, the lithium ion secondary battery 1 to which the present invention is applied includes a positive electrode 11, a negative electrode 14, a separator 17, and an electrolytic solution 18, and a container 19 that houses them and a container 19 are sealed. And a lid 20. The lid 20 is provided with a sealing plug 21 for sealing the opening of the lid.
As the constituent elements of these lithium ion secondary batteries, various substances used in general lithium ion secondary batteries can be used.

The positive electrode 11 is configured by providing a positive electrode active material layer 13 made of a lithium composite oxide on the surface of a positive electrode current collector 12 made of a conductive foil such as aluminum. As the positive electrode active material, for example, a lithium composite oxide represented by a chemical formula such as LiCoO ₂ , LiMn ₂ O ₄ , LiNiO ₂ can be used. In addition, in order to bind the positive electrode active material to the positive electrode current collector 12. The binder may contain a binder. As the binder, for example, polyvinylidene fluoride can be used.

The negative electrode 14 is configured by providing a negative electrode active material layer 16 on the surface of a negative electrode current collector 15 made of a conductive foil such as copper. As the negative electrode active material, for example, a carbon material can be used.
Further, the negative electrode current collector 15 may contain a binder (binder) in order to bind the negative electrode active material. As the binder, for example, polyvinylidene fluoride, styrene butadiene rubber (SBR) or the like can be used.

A lead made of a conductive metal is connected to the positive electrode 11 and the negative electrode 14. This lead may be configured to be electrically connected to the container 19 or the lid 20.
As the separator 17, for example, a porous film made of polyolefin, polypropylene, polyethylene or the like can be used.
The electrolytic solution 18 is formed by dissolving a lithium salt and an additive in a non-aqueous solvent. As the non-aqueous solvent, for example, cyclic carbonates such as propylene carbonate and ethylene carbonate, and chain carbonates such as ethyl methyl carbonate, dimethyl carbonate, and diethyl carbonate can be used. As the lithium salt, for example, LiPF ₆ , LiBF ₄ or the like can be used. As an additive for film formation, for example, vinylene carbonate (VC) can be used.

The container 19 may be made of metal such as aluminum, iron, and stainless steel, or may be made of resin or a laminate film. Further, the shape of the container may be a cylindrical shape or a rectangular parallelepiped shape.
The lid 20 may be a metal such as aluminum, iron, stainless steel, or the like, or may be made of resin. When used as a terminal part, a material suitable for the polarity can be selected as appropriate.

[2. Manufacturing procedure]
The manufacturing method of the lithium ion secondary battery of this invention was performed along the flowchart shown in FIG.
[2-1. Assembly process]
In the assembly process of the lithium ion secondary battery 1 according to the present invention, the positive electrode 11, the negative electrode 14, and the separator 17 are formed long (step S101), and these are overlapped and wound (step S102). Is stored in the container 19 and the lid 20 is attached (step S103), and the electrolytic solution 18 is injected into the container 19 (step S104). Or what laminated | stacked the positive electrode 11, the negative electrode 14, and the separator 17 which were formed on the flat plate may be accommodated in the container 19 (step S102).

  After the battery assembly process, moisture is removed by the moisture removal process (step S105). At the same time, the gas generated by the moisture removal process is released (step 106), and then the battery is sealed (step 107). The lithium ion secondary battery 1 is manufactured by performing film formation and charging in the initial charging process (step 108).

[2-2. Moisture removal process]
The water removal step in the method for removing water from a lithium ion secondary battery according to the present invention charges a lithium ion secondary battery by applying a voltage between a positive electrode and a negative electrode of the lithium ion secondary battery with a charge / discharge device. This is a step of removing moisture inside the lithium ion secondary battery. The present invention is characterized in that the voltage applied to the battery in the moisture removing step is periodically changed.

As shown in FIG. 1A, the water removal step includes a charging step of electrolyzing water in the battery by charging the lithium ion secondary battery (S1, S2), and an electrode by discharging the lithium ion secondary battery. It is preferable to have a discharge step (S3, S4) for removing the adsorbed gas.
In the moisture removal process, hydrogen gas and oxygen gas are generated along with the electrolysis of water. Therefore, after releasing the gas in the moisture removal process, the battery is sealed in the sealing process.
At this time, in order to avoid the moisture in the atmosphere from entering the battery when the gas is released, the sealing operation at the end of the moisture removal step is preferably performed in an environment with a small amount of moisture in the atmosphere.

(Charging step of moisture removal process)
In the charging step, as shown in FIG. 1A, charging is first performed by supplying a charging current to the lithium ion secondary battery at a constant current (step 1 (S1): constant current charging), and constant current charging. After the battery voltage of the lithium ion secondary battery reaches or exceeds the water electrolysis voltage V _W , the charging current is gradually decreased and charging is performed so that the battery voltage becomes constant at V ₂ (step 2 (S2)). : Constant voltage charging), the water in the lithium ion ion secondary battery is electrolyzed.

The charging step includes a region where charging is performed at a charging voltage that is a voltage equal to or higher than the electrolysis voltage of water and lower than the voltage at which the negative electrode film formation reaction occurs, thereby avoiding a reaction with the additive. Thus, water can be electrolyzed.
In the charging step, reactions of the following formulas (1) and (2) occur on the surfaces of the positive electrode and the negative electrode.
Positive electrode reaction H ₂ O (l) → 1 / 2O ₂ (g) + 2H ⁺ + 2e ⁻ (1)
Negative electrode reaction 2H ⁺ + 2e ⁻ → H ₂ (g) (2)
(In the above formula, (l) represents a liquid, and (g) represents a gas.)
That is, due to the electrolysis of water in the electrolytic solution, oxygen gas is generated by the reaction of the formula (1) at the positive electrode, and hydrogen gas is generated by the reaction of the formula (2) at the negative electrode. Thereby, the water | moisture content in electrolyte solution is removed.

  The current value passed in step 1 may be constant, may be increased or decreased, or may be a combination of a plurality of current values. Further, the voltage application may be performed continuously or intermittently with interruptions. Further, the current may be changed in accordance with the temperature at the time of charging. However, constant current charging is preferable from the viewpoint of facilitating voltage control.

When the battery voltage becomes equal to or higher than the water electrolysis voltage V _W by the constant current charging in step 1, the process proceeds to the constant voltage charging in step 2. Note that the timing of the transition to step 2 is the time when the voltage of the battery is measured by a sensor provided in the charging device and it is confirmed that the battery has reached a predetermined voltage. In addition, the time required to reach a predetermined voltage was measured in advance according to the charging status such as current value, battery capacity, battery type, etc., and the necessary time passed after starting constant current charging You may make it transfer to step 2 in that case.

Here, the lower limit of the charging voltage V ₂ at the time of constant voltage charging in step 2 is determined by the water electrolysis voltage V _W. That is, since water is electrolyzed by constant voltage charging, the charging voltage V ₂ is preferably equal to or higher than the water electrolysis voltage. The water electrolysis voltage V _W is about 1.23 [V]. From the viewpoint of efficiently performing electrolysis in consideration of the overvoltage component, the charging voltage V _{2 at} the time of constant voltage charging in step ₂ is usually 1. 3 [V] or more, preferably 1.6 [V] or more.

The upper limit of the charging voltage V ₂ is preferably a voltage that does not cause decomposition of the electrolytic solution, the electrolyte, and the additive. In addition, when a voltage of 3.5 V or more is applied, the reaction of the additive contained in the battery occurs, and if moisture remains in the electrolyte solution, the reaction between the moisture and the additive occurs. May affect performance. In particular, from the viewpoint of avoiding the negative electrode film formation reaction due to the additive in a state where moisture remains in the electrolyte, the charging voltage V ₂ is lower than the voltage (negative electrode film formation voltage) V _{S at} which the negative electrode film formation reaction occurs. Preferably there is. For this reason, the charging voltage V _{2 at} the time of constant voltage charging in step 2 is usually 3.5 [V] or less.

If the charging voltage V ₂ is the range of time of constant-voltage charging step 2 may be constant, increasing, it may be lowered, or may be performed by combining a plurality of voltage values. Further, the voltage application may be performed continuously or intermittently with interruptions. Further, since the electrolysis voltage V _W of water varies depending on the temperature, the charging voltage may be changed according to the temperature at the time of charging. However, from the viewpoint of keeping the voltage within the above range and preventing side reactions, constant voltage charging performed at a voltage within the above range is preferable.

The amount of water remaining in the electrolytic solution after the water removal step is preferably an amount capable of suppressing side reactions that hinder reaction with the electrolytic solution and film formation described below, and is usually 100 [ppm] or less, preferably Is 10 [ppm] or less, more preferably 5 [ppm] or less.
Moisture contained in the electrode, separator, container, etc. is eluted into the electrolytic solution after assembly, and is removed by electrolyzing the moisture in the electrolytic solution. Further, by performing electrolysis using the positive electrode and the negative electrode, moisture contained in or adhering to the electrode is also efficiently removed.

  In the method of manufacturing a lithium ion secondary battery to which the present invention is applied, it is preferable that a charge step is performed as a moisture removal step, a discharge step described later is performed, and then an initial charge step described later is performed. Moreover, after performing a charge step as a water | moisture-content removal process, it is preferable to perform the discharge step mentioned later, and also to repeat a charge step and a discharge step, and to perform the initial charge process mentioned later after that.

(Discharge step of moisture removal process)
In the moisture removal step, it is preferable to perform a step of passing a current in the opposite direction to steps 1 and 2, that is, a discharge step of discharging the lithium ion secondary battery.
In the discharging step, as shown in FIG. 1 (a), discharging at a constant current is performed (step 3 (S3): constant voltage discharging), and the battery voltage of the lithium ion secondary battery is reduced by the constant voltage discharging. The gas adsorbed on the electrode by gradually reducing the discharge current so as to be lower than the decomposition voltage V _W and discharging the battery voltage to be constant at V ₁ (step 4 (constant voltage discharge)). The reaction area of the electrode is recovered by reducing.

The discharge step includes a region where discharge is performed at a discharge voltage that is a voltage lower than the electrolysis voltage of water, thereby reducing the gas adsorbed on the electrode.
The discharge in Step 3 and Step 4 is performed by applying a load to the battery by a charge / discharge test apparatus or the like.
The current value passed in step 3 may be constant, may be increased or decreased, or may be a combination of a plurality of current values. Further, the discharge may be performed continuously or intermittently with interruptions. Further, the current may be changed in accordance with the temperature at the time of discharging. However, constant current discharge is preferable from the viewpoint of facilitating voltage control.

When the battery voltage becomes equal to or lower than the water electrolysis voltage V _W due to the constant current discharge in step 3, the process proceeds to the constant voltage discharge in step 4. Note that the timing of the transition to step 4 is the time when the voltage of the battery is measured by a sensor provided in the charging device and it is confirmed that a predetermined voltage is reached. In addition, the time required to reach a predetermined voltage was measured in advance according to the charging status such as current value, battery capacity, battery type, etc., and the necessary time passed after starting constant current charging You may make it transfer to step 4 in that case.

In the constant voltage discharge in step 4, the discharge is performed while maintaining a predetermined voltage between the positive electrode and the negative electrode, so that the discharge is performed at a voltage lower than the water electrolysis voltage V _W. The battery voltage at the time of performing constant voltage discharge in Step 4 is defined as a discharge voltage V ₁ .
Here, it is preferable that the discharge voltage V _{1 at} the time of the constant voltage discharge in step 4 is equal to or higher than a voltage for preventing the elution of the negative electrode current collector. That is, the voltage V ₁ of the constant voltage discharge is preferably larger than the voltage V _{C at} which the negative electrode current collector is eluted.

Discharge voltages V ₁ during the constant voltage discharging step 4 is within the above range may be a constant, elevated, may be lowered, or may be performed by combining a plurality of voltage values. Further, the discharge may be performed continuously or intermittently with interruptions. Moreover, you may change a voltage according to the temperature at the time of charging. However, from the viewpoint of keeping the voltage in the above range and preventing side reactions, constant voltage charging within the above range is preferable.

In step 4, when the voltage drops below the above range, charging may be performed as appropriate. That is, in order to maintain the discharge voltage within the above range, constant voltage discharge may be performed while alternately charging and discharging the battery.
As shown in FIG. 1 (b), in the moisture removal process, the gas generated from the electrolysis of water in the charging step is efficiently attached to the electrode and the gas is removed from the electrode in the discharging step. The charging step (steps 1 and 2) and the discharging step (steps 3 and 4) are preferably performed repeatedly.

  That is, in the moisture removal process, a charging step for charging the lithium ion secondary battery and electrolysis of moisture in the battery, and a discharging step for reducing the gas adhering to the electrode and discharging of the lithium ion secondary battery are alternately performed. In this way, it is possible to efficiently remove the moisture in the electrode by combining the step of removing the moisture and the step of reducing the gas generated by the moisture removal and adhering to the electrode.

  The order of performing the charging step (steps 1 and 2) and the discharging step (steps 3 and 4) is as follows. From the viewpoint of removing the gas adhering to the electrode by the charging step by the discharging step, the charging step is performed first, and then the discharging is performed. It is preferable to perform the steps. Moreover, it is preferable to perform a charge step and a discharge step alternately. Moreover, it is preferable that the last process of a moisture removal process performs a discharge step.

[2-3. Initial charging process]
The initial charging step is a step of charging the lithium ion secondary battery by applying a voltage between the positive electrode and the negative electrode of the lithium ion secondary battery and forming a film on the negative electrode of the lithium ion secondary battery.
The initial charging step can be performed in a normal atmosphere because the battery is sealed after the above-described moisture removal step.

  In the initial charging step, as shown in FIGS. 1A and 1B, after the moisture removal step, charging is first performed by supplying a charging current to the lithium ion secondary battery at a constant current (step 5 (S5)). ): Constant current charging). After the battery voltage of the lithium ion secondary battery reaches the initial upper limit voltage by constant current charging, the charging current is gradually decreased to perform charging so that the voltage becomes constant (step 6 (S6): constant voltage charging). Thus, the lithium ion ion secondary battery is charged and the negative electrode film is formed.

The film formation reaction is a reaction that forms a film on the surface of the negative electrode by the reaction of the electrolytic solution and the additive in the electrolytic solution on the negative electrode. By forming the negative electrode film, the electric capacity and cycle characteristics can be improved.
The constant current charging in step 5 is performed by passing a current having a predetermined current value between the positive electrode and the negative electrode, as in step 1.

When the battery voltage reaches the initial charge upper limit voltage V ₃ by the constant current charge in step 5, the process proceeds to the constant voltage charge in step 6. Note that the timing of the transition to step 6 is the time when the voltage of the battery is measured by a sensor provided in the charging device and it is confirmed that a predetermined voltage has been reached. In addition, the time required to reach a predetermined voltage was measured in advance according to the charging status such as current value, battery capacity, battery type, etc., and the necessary time passed after starting constant current charging You may make it transfer to step 6 in that case.

In the constant voltage charging in Step 6, as in Step 2, the voltage V ₃ is applied by flowing a current so as to maintain a predetermined voltage between the positive electrode and the negative electrode. The battery voltage at the time of performing constant voltage charging in Step 6 is set as the initial charging upper limit voltage V ₃ .
Here, the initial charge upper limit voltage V ₃ , which is the charge voltage at the time of constant voltage charging in step 6, is higher than the voltage (negative electrode film formation voltage) V _{S at} which the reaction of the additive for forming the negative electrode film occurs. Is preferred.

  If moisture remains in the electrolyte during the reaction of the additive, the reaction of the additive and the formation of the film are affected. For this reason, it is necessary to remove moisture and reduce moisture before forming the coating. In the method of manufacturing a lithium ion secondary battery to which the present invention is applied, a good film forming reaction proceeds by performing charging at or above the reaction voltage of the additive in Steps 5 and 6 after removing moisture.

[3. Embodiment]
Next, detailed embodiments of the present invention will be described. These embodiments may be performed alone or in appropriate combinations.
[Embodiment 1]
Fig.2 (a) is a figure explaining control of the battery voltage in the first charge by the manufacturing method of the lithium ion secondary battery which concerns on this embodiment.
In the method for manufacturing a lithium ion secondary battery according to this embodiment, the lithium ion secondary battery having the above-described configuration is assembled by the above-described assembly process. The first charge is performed on the assembled lithium ion secondary battery.

In the initial charging of the method for manufacturing a lithium ion secondary battery according to the present embodiment, moisture is removed from the lithium ion secondary battery by applying a voltage between the positive electrode and the negative electrode of the lithium ion secondary battery. A moisture removing step and an initial charging step of forming a film on the negative electrode, and the moisture removing step is performed independently before the initial charging step.
Here, the moisture removal step is a step of applying a voltage that is equal to or higher than the water electrolysis voltage and lower than the voltage at which the negative electrode film formation reaction occurs to the lithium ion secondary battery.

The initial charging step is a step of applying a voltage equal to or higher than the voltage at which the negative electrode film forming reaction occurs to the lithium ion secondary battery.
Furthermore, an initial charge process is performed by applying a voltage continuously to the voltage at which the negative electrode film formation reaction occurs after the moisture removing process.
That is, constant current charging is performed until the battery voltage reaches a charging voltage V ₂ that is higher than the water electrolysis voltage V _{W and} lower than the negative electrode film forming voltage V _S (0 to t _a1 ), and reaches the voltage value V ₂ . After reaching, constant voltage charging is performed with the charging voltage V ₂ (t _{a1 to} t _a2 ). Next, constant current charging is performed until the battery voltage reaches the initial charge upper limit voltage V ₃ equal to or higher than the negative electrode film forming voltage V _S (t _{a2 to} t _a3 ), and after reaching the voltage value V ₃ , the initial charge upper limit voltage V ₃ performs constant voltage charging (from t _a3 ).

  By performing such initial charging, the present embodiment allows the moisture in the battery to flow before the negative electrode film formation reaction occurs by applying a voltage that is equal to or higher than the electrolysis voltage of water and lower than the negative electrode film formation voltage. The film formation reaction is performed after removing the moisture and removing the moisture. In other words, a good negative electrode film is formed by preventing the side reaction caused by the film formation in the presence of moisture by independently performing the water removal in the moisture removal process and the film formation in the initial charging process. And the characteristics of the lithium ion secondary battery can be improved. In addition, since the initial charging process is continuously performed after the moisture removing process, the time required for the initial charging can be reduced. Furthermore, since the control of the charging voltage is easy, the configuration of the charger used for charging can be simplified.

[Embodiment 2]
FIG. 2B is a diagram for explaining the control of the battery voltage in the initial charge by the method for manufacturing the lithium ion secondary battery according to the present embodiment.
In the method for manufacturing a lithium ion secondary battery according to the present embodiment, as in Example 1, the lithium ion secondary battery is assembled. Further, the assembled lithium ion secondary battery is charged for the first time.

In the initial charge of the method of manufacturing a lithium ion secondary battery according to the present embodiment, a moisture removal step of removing moisture inside the lithium ion secondary battery by applying a voltage to the lithium ion secondary battery, and moisture removal An initial charging step of forming a film on the negative electrode after the step, and changing the voltage applied to the battery in the moisture removal step.
Here, the water removal step is a charge step of charging at a charge voltage that is a voltage equal to or higher than the water electrolysis voltage and lower than the voltage at which the negative electrode film formation reaction occurs, and the water electrolysis voltage. A discharge step for discharging at a lower discharge voltage is provided, and the charge step and the discharge step are alternately performed.

In the charging step, constant current charging is performed at a predetermined current value until the battery voltage reaches the charging voltage, and constant voltage charging is performed at the charging voltage when the battery voltage reaches the charging voltage. In the discharging step, constant current discharge is performed at a predetermined current value until the battery voltage reaches the discharge voltage, and constant voltage discharge is performed at the discharge voltage when the battery voltage reaches the discharge voltage.
That is, constant current charging is performed until the battery voltage reaches a charging voltage V ₂ that is higher than the water electrolysis voltage V _{W and} lower than the negative electrode coating forming voltage V _S (0 to t _b1 ). after reaching V ₂ performs constant voltage charging by the charging voltage _{V 2 (t b1 ~t b2)} . Next, constant current discharge is performed until the battery voltage is lower than the water electrolysis voltage V _W and becomes a discharge voltage V ₁ greater than the voltage V _{C at} which the negative electrode current collector is eluted (t _{b2 to} t _b3 ) After reaching the voltage value V ₁ , constant voltage discharge is performed with the discharge voltage V ₁ (t _{b3 to} t _b4 ). Further, similarly, constant voltage charging with the charging voltage V ₂ and constant voltage discharging with the discharging voltage V ₁ are repeated (t _{b4 to} t _b16 ). Thereafter, constant current charging is performed until the battery voltage reaches the initial charge upper limit voltage V ₃ equal to or higher than the negative electrode film forming voltage V _S (t _{b16 to} t _b17 ), and after reaching the voltage value V ₃ , the initial charge upper limit voltage V ₃ is reached. Thus, constant voltage charging is performed ( _tb17- ).

  By performing such initial charging, the present embodiment can perform water removal in the water removal step and film formation in the independent initial charging step independently as in the first embodiment. Further, by repeating the charging step and the discharging step, the gas adhering to the electrode surface in the charging step can be removed in the discharging step, so that the efficiency of moisture removal can be increased. Thereby, a favorable negative electrode film can be formed and the characteristic of a lithium ion secondary battery can be improved.

[Embodiment 3]
FIG.2 (c) is a figure explaining control of the battery voltage in the first charge by the manufacturing method of the lithium ion secondary battery which concerns on this embodiment.
In the method for manufacturing a lithium ion secondary battery according to the present embodiment, as in Example 1, the lithium ion secondary battery is assembled. Further, the assembled lithium ion secondary battery is charged for the first time.

The initial charging of the method for manufacturing a lithium ion secondary battery according to the present embodiment is performed in the same manner as the initial charging of the second embodiment. Further, as the elapsed time from the start of charging increases, constant voltage charging and / or constant charging is performed. By extending the voltage discharge time, the period from the start of the charge step to the start of the next charge step is lengthened.
That is, as in the second embodiment, constant current charging is performed until the battery voltage reaches a charging voltage V ₂ that is higher than the water electrolysis voltage V _{W and} lower than the negative electrode film forming voltage V _S (0 to t _c1 ), after reaching the voltage value _{V 2} performs constant voltage charging by the charging voltage _{V 2 (t c1 ~t c2)} . Next, constant current discharge is performed until the battery voltage reaches a discharge voltage V ₁ that is lower than the electrolysis voltage V _{W of} water and greater than the voltage V _{C at} which the negative electrode current collector is eluted (t _{c2 to} t _c3 ) After reaching the voltage value V ₁ , constant voltage discharge is performed with the discharge voltage V ₁ (t _{c3 to} t _c4 ). Further, in the same manner, the constant voltage charging by the charging voltage _{V 2 (t c5 ~t c6,} t c9 ~t c10, t c13 ~t c14) and the constant voltage discharge by the discharge voltage _{V 1} (t _c7 ~t _{c8, t c11 ~t c12, t c15 ~t} c16) is repeated (t _c4 ~t _c16), the charging time in one time of charging step and discharging step (t _c1 ~t _c2) or discharging time (t _c3 ~t _c4 ) Longer than the charging time (t _{c5 to} t _c6 ) or discharging time (t _{c7 to} t _c8 ) in the second charging step and discharging step, and thereafter repeating the moisture removal process, As it increases, the charging time and discharging time are lengthened. Thereafter, constant current charging is performed until the battery voltage reaches the initial charge upper limit voltage V ₃ equal to or higher than the negative electrode film forming voltage V _S (t _{c16 to} t _c17 ), and after reaching the voltage value V ₃ , the initial charge upper limit voltage V ₃ is reached. To perform constant voltage charging (t _c17 ˜).

  By performing such initial charging, the present embodiment can perform water removal in the water removal step and film formation in the initial charge step independently as in the first embodiment. Further, by repeating the charging step and the discharging step in the same manner as in the second embodiment, the gas adhering to the electrode surface in the charging step can be removed in the discharging step, so that the efficiency of moisture removal can be improved.

  By repeatedly performing the water removal step, the amount of water contained in the electrolytic solution decreases. In the present embodiment, by increasing the charging time as the elapsed time of charging increases, it becomes possible to conduct the reaction by attracting moisture present in the electrolyte more to the electrode, and the efficiency of moisture removal Can be increased. Thereby, a favorable negative electrode film can be formed and the characteristic of a lithium ion secondary battery can be improved.

[Embodiment 4]
FIG. 3A is a diagram for explaining the control of the battery voltage in the initial charge by the method for manufacturing a lithium ion secondary battery according to the present embodiment.
In the method for manufacturing a lithium ion secondary battery according to the present embodiment, as in Example 1, the lithium ion secondary battery is assembled. Further, the assembled lithium ion secondary battery is charged for the first time.

In the initial charging of the method for manufacturing a lithium ion secondary battery according to the present embodiment, the charging is performed in the same manner as the initial charging in the second embodiment, and the charging voltage is increased as the elapsed time from the start of charging increases.
That is, the battery voltage is higher than the electrolysis voltage V _W of water, a constant current charging until the charging voltage lower V _d21 than the negative film forming voltage V _S (0~t _d1), the voltage value V _d21 After reaching, constant voltage charging is performed with the charging voltage V _d21 (t _{d1 to} t _d2 ). Next, constant current discharge is performed until the battery voltage becomes a discharge voltage V ₁ that is lower than the electrolysis voltage V _{W of} water and greater than the voltage V _{C at} which the negative electrode current collector is eluted (t _{d2 to} t _d3 ), after reaching the voltage value V ₁ performs the constant voltage discharge by the discharge voltage _{V 1 (t d3 ~t d4)} . Further, in the same manner, constant voltage charging and constant voltage discharging by the discharge voltage V ₁ are performed (t _{d4 to} t _d16 ), but the charging voltage V _d21 of the first charging step (t _{d1 to} t _d2 ) The charging voltage V _d22 of the second charging step ((t _{d5 to} t _d6 ) is increased, and thereafter the water removal process is repeated in the same manner, and the charging voltage of the charging step is increased as the elapsed time of charging increases. Thereafter, constant current charging is performed until the battery voltage reaches the initial charge upper limit voltage V ₃ equal to or higher than the negative electrode film forming voltage V _S (t _{d16 to} t _d17 ), and after reaching the voltage value V ₃ , the initial charge upper limit voltage V _The constant voltage charging is performed by ₃ ( _td17- ).

  By performing such initial charging, the present embodiment can perform water removal in the water removal step and film formation in the initial charge step independently as in the first embodiment. Further, by repeating the charging step and the discharging step in the same manner as in the second embodiment, the gas adhering to the electrode surface in the charging step can be removed in the discharging step, so that the efficiency of moisture removal can be improved.

  The higher the charging voltage, the more efficiently the water contained in the battery can be removed, but the amount of water in the battery is high immediately after the start of the initial charging, so the side voltage of the additive is avoided to increase the charging voltage. It is not possible. On the other hand, according to the present embodiment, immediately after the start of the initial charge, the charge voltage is lowered, the moisture removal proceeds, and the charge voltage is increased as the moisture in the electrolyte decreases, so that the additive Water can be efficiently removed while avoiding side reactions. Thereby, a favorable negative electrode film can be formed and the characteristic of a lithium ion secondary battery can be improved.

  In this embodiment, since the moisture contained in the electrolytic solution is reduced by repeating the moisture removing step, the charging voltage is increased to the voltage at which the negative electrode film is formed because the charging time is shortened. Alternatively, the initial upper limit voltage may be increased.

[Embodiment 5]
FIG. 3B is a diagram for explaining the control of the battery voltage in the initial charging by the method for manufacturing a lithium ion secondary battery according to the present embodiment.

In the method for manufacturing a lithium ion secondary battery according to the present embodiment, as in Example 1, the lithium ion secondary battery is assembled. Further, the assembled lithium ion secondary battery is charged for the first time.
The initial charging of the method for manufacturing a lithium ion secondary battery according to the present embodiment is performed in the same manner as the initial charging in the second embodiment, and the discharge voltage is increased as the elapsed time from the start of charging increases.

That is, the battery voltage is higher than the electrolysis voltage V _W of water, a constant current charging until the charging voltage lower V ₂ than the negative film forming voltage V _S (0~t _e1), the voltage value V ₂ After reaching, constant voltage charging is performed with the charging voltage V ₂ (t _{e1 to} t _e2 ). Next, constant current discharge is performed until the _battery voltage becomes a discharge voltage V _e11 lower than the water electrolysis voltage V _{W and} higher than the voltage V _{C at} which the negative electrode current collector is eluted (t _{e2 to} t _e3 ) After reaching the voltage value V _e11 , constant voltage discharge is performed with the discharge voltage V _e11 (t _{e3 to} t _e4 ). Further, in the same manner, constant voltage charging by the charging voltage V ₂ and constant voltage discharging are repeated (t _{e4 to} t _e16 ), but the discharging voltage V _e11 of the first discharging step (t _{e3 to} t _e4 ) a discharge voltage V _e12 of the second discharge step (t _e7 ~t _e8) increased similarly repeated water removing step after, as the elapsed time of charging is increased, than the electrolysis voltage V _W of water Increase the discharge voltage of the discharge step within a small range. Thereafter, constant current charging is performed until the battery voltage reaches the initial charge upper limit voltage V ₃ equal to or higher than the negative electrode film forming voltage V _S (t _{e16 to} t _e17 ), and after reaching the voltage value V ₃ , the initial charge upper limit voltage V ₃ performs constant voltage charging (from t _e17 ).

  By performing such initial charging, the present embodiment can perform water removal in the water removal step and film formation in the initial charge step independently as in the first embodiment. Further, by repeating the charging step and the discharging step in the same manner as in the second embodiment, the gas adhering to the electrode surface in the charging step can be removed in the discharging step, so that the efficiency of moisture removal can be improved.

  When the battery voltage is low, the negative electrode current collector may be eluted. Immediately after the electrolytic solution is injected into the battery and the assembly process is completed, the current collector is unlikely to elute, but the current collector is likely to elute over time after the electrolytic solution is injected. Therefore, according to the present embodiment, the time elapses after the electrolyte solution is injected, and the current collector is less likely to be eluted. By increasing the discharge voltage as the body is more likely to elute, it is possible to reduce the influence of the current collector on the elution and to remove moisture. Thereby, a favorable negative electrode film can be formed and the characteristic of a lithium ion secondary battery can be improved.

[Embodiment 6]
FIG.3 (c) is a figure explaining control of the battery voltage in the first charge by the manufacturing method of the lithium ion secondary battery which concerns on this embodiment.
In the method for manufacturing a lithium ion secondary battery according to the present embodiment, as in Example 1, the lithium ion secondary battery is assembled. Further, the assembled lithium ion secondary battery is charged for the first time.

In the initial charging of the manufacturing method of the lithium ion secondary battery according to the present embodiment, the charging is performed in the same manner as the initial charging of the second embodiment, and further, the charging voltage and the discharging voltage are increased as the elapsed time from the start of charging increases. Raise.
That is, the battery voltage is higher than the electrolysis voltage V _W of water, a constant current charging until the charging voltage lower V _f21 than negative film forming voltage V _S (0~t _f1), the voltage value V _f21 After reaching, constant voltage charging is performed with the charging voltage V _f21 (t _{f1 to} t _f2 ). Next, constant current discharge is performed until the battery voltage becomes a discharge voltage V _f11 that is lower than the water electrolysis voltage V _{W and} greater than the voltage V _{C at} which the negative electrode current collector is eluted (t _{f2 to} t _f3 ) After reaching the voltage value V _f11 , constant voltage discharge is performed with the discharge voltage V _f11 (t _{f3 to} t _f4 ). Further, in the same manner, the constant voltage charging are repeated a constant voltage discharge (t _f4 ~t _f16) is charged than the voltage V _f21, 2 nd charging step of first charge step (t _f1 ~t _f2) The charging voltage V _f22 of (t _{f5 to} t _f6 ) is increased, and thereafter the moisture removal process is repeated in the same manner, and the charging step charging voltage is increased as the elapsed time of charging increases. In addition, the charge voltage V _f12 of the second charge step (t _{f7 to} t _f8 ) is made larger than the discharge voltage V _f11 of the first discharge step (t _{f3 to} t _f4 ), and the water removal process is similarly performed thereafter. Repeatedly, as the elapsed time of charging increases, the discharge voltage in the discharge step is increased in a range smaller than the water electrolysis voltage V _W. Thereafter, constant current charging is performed until the battery voltage reaches the initial charge upper limit voltage V ₃ equal to or higher than the negative electrode film forming voltage V _S (t _{f16 to} t _f17 ), and after reaching the voltage value V ₃ , the initial charge upper limit voltage V ₃ is reached. To perform constant voltage charging ( _tf17- ).

  By performing such initial charging, the present embodiment can perform water removal in the water removal step and film formation in the initial charge step independently as in the first embodiment. Further, by repeating the charging step and the discharging step in the same manner as in the second embodiment, the gas adhering to the electrode surface in the charging step can be removed in the discharging step, so that the efficiency of moisture removal can be improved.

  Furthermore, as in the fourth embodiment, it is possible to efficiently remove water while avoiding side reactions of the additives, and to remove water with less influence on the elution of the current collector as in the fifth embodiment. It becomes possible. Thereby, a favorable negative electrode film can be formed and the characteristic of a lithium ion secondary battery can be improved.

DESCRIPTION OF SYMBOLS 1 Lithium ion secondary battery 11 Positive electrode 12 Positive electrode collector 13 Positive electrode active material layer 14 Negative electrode 15 Negative electrode collector 16 Negative electrode active material layer 17 Separator 18 Electrolytic solution 19 Container 20 Lid 21 Seal plug

Claims (2)

A method for removing moisture contained in a lithium ion secondary battery comprising a positive electrode, a negative electrode, a separator, and an electrolyte solution,
The positive electrode current collector is aluminum;
The current collector of the negative electrode is copper;
A moisture removal step of removing moisture inside the lithium ion secondary battery by applying a voltage to the lithium ion secondary battery;
The moisture removal step includes
A charging step including a region where charging is performed at a charging voltage that is a voltage equal to or higher than an electrolysis voltage of water and lower than a voltage at which a negative electrode film formation reaction occurs;
A discharge step including a region where discharge is performed at a discharge voltage that is lower than the electrolysis voltage of water;
In the moisture removal step, alternately performing the charging step and the discharging step, periodically changing the voltage applied to the lithium ion secondary battery,
As the elapsed time from the start of charging increases, the discharge voltage is increased ,
The method for removing moisture from a lithium ion secondary battery, wherein the discharge voltage is a voltage higher than a voltage at which copper as the current collector of the negative electrode elutes . In the charging step, constant current charging is performed at a predetermined current value until the battery voltage reaches the charging voltage, and constant voltage charging is performed at the charging voltage when the battery voltage reaches the charging voltage,
In the discharging step, constant current discharge is performed at a predetermined current value until the battery voltage reaches the discharge voltage, and constant voltage discharge is performed at the discharge voltage when the battery voltage reaches the discharge voltage. The method for removing moisture from a lithium ion secondary battery according to claim 1.

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