The following description relates to a method for manufacturing a rechargeable battery and an apparatus for manufacturing a rechargeable battery.
A rechargeable battery, such as a lithium-ion rechargeable battery, typically includes an electrode plate formed by applying an electrode mixture including an electrode active material to a substrate that becomes a current collector. In such a rechargeable battery, the specific surface area of the electrode active material included in the electrode mixture greatly affects the battery performance. Accordingly, Japanese Laid-Open Patent Publication No. 2005-19094 describes an example of a preferred range of the specific surface area of an electrode active material forming a negative electrode. Japanese Laid-Open Patent Publication No. 9-175825 describes an example of the relationship between a firing temperature of a precursor of an electrode active material and the specific surface area of an electrode active material.
Further, the electrode active material, serving as a raw material of the electrode mixture, usually tolerates variations in the specific surface area within a predetermined range. In a state in which the electrode mixture applied to a substrate forms an electrode plate, the specific surface area of the electrode active material is referred to an electrode plate specific surface area. Taking into consideration uniformity of the battery performance, it is preferred that variations of the electrode plate specific surface area be minimized.
This Summary is provided to introduce a selection of concepts in a simplified form that are further described below in the Detailed Description. This Summary is not intended to identify key features or essential features of the claimed subject matter, nor is it intended to be used as an aid in determining the scope of the claimed subject matter.
In one general aspect, a method for manufacturing a rechargeable battery includes applying an electrode mixture that includes an electrode active material to a substrate that becomes a current collector, drying the applied electrode mixture, obtaining a specific surface area of the electrode active material before the drying the applied electrode mixture, in which the obtained specific surface area of the electrode active material is referred to as an obtained specific surface area, and a specific surface area of the electrode active material in a state in which the electrode mixture applied to the substrate forms an electrode plate is referred to as an electrode plate specific surface area; and adjusting the electrode plate specific surface area after the drying the applied electrode mixture by setting a drying condition of the electrode mixture in accordance with the obtained specific surface area.
In the above method, a drying temperature of the electrode mixture may be set as the drying condition. The drying temperature may be set to be higher as the obtained specific surface area becomes smaller.
In the above method, a drying time of the electrode mixture may be set as the drying condition. The drying time may be set to be longer as the obtained specific surface area becomes smaller.
In the above method, the drying condition may be set based on a change amount of the electrode plate specific surface area that varies in accordance with the drying condition so as to correct a difference of the obtained specific surface area and a predetermined standard specific surface area.
The above method may further include blending raw materials of the electrode mixture, and kneading the blended electrode mixture. The kneaded electrode mixture may be applied to the substrate. The specific surface area of the electrode active material obtained before the blending raw materials may serve as the obtained specific surface area.
In another general aspect, an apparatus for manufacturing a rechargeable battery applies an electrode mixture that includes an electrode active material to a substrate that becomes a current collector and dries the applied electrode mixture. A specific surface area of the electrode active material obtained before the electrode mixture is dried is referred to as an obtained specific surface area. A specific surface area of the electrode active material in a state in which the electrode mixture applied to the substrate forms an electrode plate is referred to as an electrode plate specific surface area. The apparatus includes an obtained specific surface area receiving unit and a drying condition calculator. The obtained specific surface area is input to the obtained specific surface area receiving unit. The drying condition calculator calculates a drying condition of the electrode mixture in accordance with the input obtained specific surface area to adjust the electrode plate specific surface area after the electrode mixture is dried.
Other features and aspects will be apparent from the following detailed description, the drawings, and the claims.
Throughout the drawings and the detailed description, the same reference numerals refer to the same elements. The drawings may not be to scale, and the relative size, proportions, and depiction of elements in the drawings may be exaggerated for clarity, illustration, and convenience.
This description provides a comprehensive understanding of the methods, apparatuses, and/or systems described. Modifications and equivalents of the methods, apparatuses, and/or systems described are apparent to one of ordinary skill in the art. Sequences of operations are exemplary, and may be changed as apparent to one of ordinary skill in the art, with the exception of operations necessarily occurring in a certain order. Descriptions of functions and constructions that are well known to one of ordinary skill in the art may be omitted.
Exemplary embodiments may have different forms, and are not limited to the examples described. However, the examples described are thorough and complete, and convey the full scope of the disclosure to one of ordinary skill in the art.
An embodiment related to a method for manufacturing a rechargeable battery will now be described with reference to the drawings.
As shown in
Specifically, the rechargeable battery 1 of the present embodiment includes a stack of sheets of the positive electrode 3, the negative electrode 4, and the separator 5. The stack of the positive electrode 3, the negative electrode 4, and the separator 5 is rolled to form the electrode body 10 in which the positive electrode 3, the negative electrode 4, and the separator 5 are alternately arranged with the separator 5 held in between in a radial direction.
Further, the case 20 of the present embodiment includes a flat box-shaped case body 21 and a lid 22 that closes an open end 21x of the case body 21. The electrode body 10 of the present embodiment has a flattened shape that corresponds to the box-shape of the case 20.
More specifically, as shown in
Specifically, in an electrode sheet 35P of the positive electrode 3, a mixture paste 37P including a lithium transition metal oxide is applied to a substrate 36P including aluminum and the like. The mixture paste 37P serves as the positive electrode active material. The substrate 36P forms a positive electrode current collector 31P of the electrode sheet 35P. Also, in an electrode sheet 35N of the negative electrode 4, a mixture paste 37N including a carbon-base material is applied to a substrate 36N including copper and the like. The mixture paste 37N serves as the negative electrode active material. The substrate 36N forms a negative electrode current collector 31N of the electrode sheet 35N. Further, the mixture pastes 37P and 37N each include a binder. In the rechargeable battery 1 of the present embodiment, the mixture pastes 37P and 37N are dried to form a positive electrode active material layer 32P and a negative electrode active material layer 32N on the positive and negative electrode sheets 35P and 35N, respectively.
In the rechargeable battery 1 of the present embodiment, the positive and negative electrode sheets 35P and 35N are shaped as strips. The electrode body 10 of the present embodiment is formed by rolling the stack of the positive and negative electrode sheets 35P and 35N with the separator 5 held in between about a rolling axis L that extends in a widthwise direction (sideward direction in
In
As shown in
Specifically, the electrode body 10 of the present embodiment is accommodated in the case 20 so that the rolling axis L is parallel to a longitudinal direction (sideward direction in
An electrolyte 41 is injected into the case 20. The rechargeable battery 1 of the present embodiment uses a fluorine-based electrolyte 41 in which lithium salt, serving as a supporting electrolyte, is dissolved in an organic solvent. In the rechargeable battery 1 of the present embodiment, the electrode body 10 is impregnated with the electrolyte 41 sealed in the case 20.
Electrode Sheet Manufacturing Process
As the flowchart shown in
Then, the electrode mixture 50 kneaded in step 102 is applied to the substrate 36P as the mixture paste 37P, and the electrode mixture 50 kneaded in step 102 is applied to the substrate 36N as the mixture paste 37N (step 103, refer to
Electrode Sheet Manufacturing Process and Specific Surface Area of Electrode Active Material
As shown in
Specifically, when specific surface area S of the electrode active material before blending the raw materials (refer to
The specific surface area of porous powder such as the electrode active material is measured by, for example, a gas adsorption measurement method using a Brunauer-Emmett-Teller (BET) equation, that is, a BET method. The unit used is “square meter/gram”. The specific surface area measured by the BET method will be referred to as the “BET specific surface area”. In the present embodiment, measure specific surface area S of the electrode active material is measured by a BET method that uses nitrogen as the gaseous adsorbate.
More specifically, as shown in
Also, as shown in
Normally, particles of the binder 56 moved toward the upper surface 50s as a result of the migration aggregate between particles of the electrode active material 55. Such segregated state of the binder 56 resulting from the migration may be expressed by “ratio (front surface side/substrate side)” as “migration index”, in which the electrode mixture 50 applied to the substrate 36 is divided into the side of the upper surface 50s and the side of the substrate 36.
Further, the pressing step squeezes the electrode active material 55 in the electrode mixture 50 and increases specific surface area S of the electrode active material 55. Thus, post-pressing electrode plate specific surface area Se3 is greater than post-drying electrode plate specific surface area Se2 (refer to
As shown in
Specifically, waveform 61 shown in
Also, as shown in
In the graph shown in
Further, as shown in
However, taking into consideration uniformity of the battery performance, it is preferred that variations of specific surface area S of the electrode active material 55 included in the electrode mixture 50 be minimized. Accordingly, in the rechargeable battery 1 of the present embodiment, a manufacturing condition for the manufacture of the electrode sheet 35 is set in accordance with specific surface area S of the electrode active material 55. Specifically, in the present embodiment, drying temperature T is set as the subject of a drying condition of the electrode mixture 50 to become higher as obtained specific surface area Sd decreases. This adjusts specific surface area S of the electrode active material 55 in a state in which the electrode mixture 50 applied to the substrate 36 forms the electrode plate 51, thereby improving uniformity of the battery performance.
In the rechargeable battery 1 of the present embodiment having a structure of a lithium-ion rechargeable battery, the battery performance is likely to be affected by variations of specific surface area S of the electrode active material 55 on the negative electrode 4 that receives lithium ions from the positive electrode 3 when charging the rechargeable battery 1. Therefore, in the present embodiment, the manufacturing condition is set in accordance with specific surface area S of the electrode active material 55 for the manufacture of the electrode sheet 35N of the negative electrode 4.
Setting Drying Condition in Accordance with Obtained Specific Surface Area
The drying condition is set in accordance with the obtained specific surface area of the electrode active material 55 when manufacturing the rechargeable battery 1 of the present embodiment.
As shown in
As shown in
As shown in
Accordingly, in the rechargeable battery 1 of the present embodiment, drying temperature T is set in accordance with obtained specific surface area Sd to adjust post-drying electrode plate specific surface area Se2. Consequently, this reduces variations of specific surface area S of the electrode active material 55 included in the electrode mixture 50 applied to the substrate 36.
Specifically, for example, as shown in
Even in these cases, if the manufacturing condition, such as the drying condition, remains the same, change amount ΔS of electrode plate specific surface area Se resulting from drying the electrode mixture 50 is substantially equal, as described above (refer to
Based on these relationships, target drying change amount ΔST for correcting difference δ of obtained specific surface area Sd and standard specific surface area Sc can be calculated with respect to change amount ΔS of electrode plate specific surface area Se resulting from drying the electrode mixture 50 applied to the substrate 36. This allows drying temperature T to be set to reduce variations of post-drying electrode plate specific surface area Se2 caused by differences in initial specific surface area S0 serving as obtained specific surface area Sd.
Under a predetermined drying condition, change amount ΔS of electrode plate specific surface area Se resulting from drying the electrode mixture 50 is referred to as reference change amount ΔSC. Further, for example, difference δ of obtained specific surface are Sd and standard specific surface area Sc is represented by “δ=Sd−Sc”, and the value obtained by subtracting difference δ of obtained specific surface area Sd and standard specific surface area Sc from reference change amount ΔSC is referred to as target drying change amount ΔST (ΔST=ΔSC−δ). Then, drying temperature T is set based on target drying change amount ΔST so as to correct difference δ of obtained specific surface area Sd and standard specific surface area Sc.
Specifically, in the example shown in
Also, in this example, initial specific surface area S0, which serves as obtained specific surface area Sd, tolerates variations within “±0.4” as tolerance α. Thus, for example, when the difference of initial specific surface area S0 and standard specific surface area Sc corresponds to the lower limit of the tolerable range (6=−0.4), target drying change amount ΔST becomes “0.5” (“ΔST=0.5”, refer to
In this manner, in the present embodiment, drying temperature T serving as the drying condition is set based on change amount ΔS of electrode plate specific surface area Se that varies in accordance with the drying condition so as to correct difference δ of obtained specific surface area Sd and standard specific surface area Sc.
Drying Condition Setting Device
A drying condition setting device used for manufacturing the rechargeable battery 1 will now be described.
As shown in
Specifically, initial specific surface area S0 of the electrode active material 55 obtained in the blending step (refer to
Specifically, as shown in
Next, the drying condition setting device 71 refers to the data table 77 held in the memory region 78 and calculates drying temperature T that corrects difference δ of obtained specific surface area Sd and standard specific surface area Sc (step 306). Then, the drying condition setting device 71 of the present embodiment is configured to output the setting of drying temperature T obtained in step 306 (step 307).
Operation
When the electrode mixture 50 applied to the substrate 36 is dried, post-drying electrode plate specific surface area Se2 becomes greater than pre-drying electrode plate specific surface area Se1. Further, change amount ΔS of electrode plate specific surface area Se resulting from drying the electrode mixture 50 is affected by the drying condition of the electrode mixture 50 applied to the substrate 36. This allows post-drying electrode plate specific surface area Se2 to be adjusted based on the setting of the drying condition.
The present embodiment has the following advantages.
The above configuration readily reduces variations of electrode plate specific surface area Se, or specific surface area S of the electrode active material 55 in a state in which the electrode mixture 50 applied to the substrate 36 forms the electrode plate 51, without complicating the configuration. This improves uniformity of the battery performance.
Specifically, change amount ΔS of electrode plate specific surface area Se resulting from drying the electrode mixture 50 increases as drying temperature T of the electrode mixture 50 applied to the substrate 36 becomes higher. Thus, the above configuration readily adjusts post-drying electrode plate specific surface area Se2 by using drying temperature T of the electrode mixture 50 as the subject of the drying condition that is set in accordance with obtained specific surface area Sd of the electrode active material 55. This reduces variations of electrode plate specific surface area Se and improves uniformity of the battery performance.
The above configuration accurately adjusts post-drying electrode plate specific surface area Se2. This reduces variations of electrode plate specific surface area Se and improves uniformity of the battery performance effectively.
Typically, the electrode active material 55 in a state of an unblended raw material tolerates variations in initial specific surface area S0 within the predetermined tolerance α. Accordingly, initial specific surface area S0 of the electrode active material 55 in the state of an unblended raw material varies between manufacturing units, or lots. Thus, the above configuration adjusts post-drying electrode plate specific surface area Se2 by setting the drying condition in accordance with obtained specific surface area Sd of the electrode active material 55 efficiently and accurately. This reduces variations of electrode plate specific surface area Se and improves uniformity of the battery performance effectively.
Furthermore, the measurement value of initial specific surface area S0 of the electrode active material 55 is often indicated in the form of specifications, labels, or the like. Thus, with the above configuration, specific surface area S of the electrode active material 55 included in the electrode mixture 50 can be easily obtained before the step of drying the electrode mixture 50 applied to the substrate 36 without performing a special measurement task. In this manner, the drying condition is efficiently set in accordance with obtained specific surface area Sd of the electrode active material 55.
The above embodiment may be modified as described below. The above embodiment and the following modifications can be combined as long as the combined modifications remain technically consistent with each other.
In the above embodiment, initial specific surface area S0, which is specific surface area S of the electrode active material 55 as a raw material of the electrode mixture 50, is obtained in the blending step of the electrode mixture 50. Then, initial specific surface area S0 is used as obtained specific surface area Sd in setting the drying condition in accordance with obtained specific surface area Sd. However, there is no limit to such a configuration as long as obtained specific surface area Sd is specific surface area S of the electrode active material 55 that is obtained before the step of drying the electrode mixture 50 applied to the substrate 36. For example, pre-drying electrode plate specific surface area Se1 may be measured and the measurement value may be used as obtained specific surface area Sd. Alternatively, specific surface area S after kneading the electrode mixture 50 may be measured before the electrode mixture 50 is applied to the substrate 36, and the measurement value may be used as obtained specific surface area Sd. Further, standard specific surface area Sc may only specify the value at the time of acquisition.
The value of standard specific surface area Sc may be set in any manner. Also, the values within tolerance α may be set in any manner. For example, the plus tolerance α may differ from the minus tolerance α. That is, standard specific surface area Sc does not have to be the standard center value.
In the above embodiment, standard specific surface area Sc serving as the standard center value is set to “4.2”, and standard drying temperature T corresponding to when obtained specific surface area Sd is equal to standard specific surface area Sc is set to “175° C.”. Then, the value of reference change amount ΔSC obtained is “0.1”. However, there is no limit to such a configuration as long as reference change amount ΔSC is a value indicating change amount ΔS of electrode plate specific surface area Se resulting from drying the electrode mixture 50 under a predetermined drying condition. Specifically, the drying condition for setting reference change amount ΔSC includes standard drying temperature T and may be changed in any manner.
In the above embodiment, the drying condition setting device 71 refers to the data table 77 held in the memory region 78 and calculates drying temperature T so as to correct difference δ of obtained specific surface area Sd and standard specific surface area Sc. The data table 77 stores in advance the relationship between difference δ of obtained specific surface area Sd and standard specific surface area Sc, target drying change amount ΔST, and drying temperature T set as the drying condition.
However, there is no limit to such a configuration. For example, as shown in
Alternatively, the drying condition setting device 71 may use data table 77 storing the relationship between difference δ of obtained specific surface area Sd and standard specific surface area Sc and drying temperature T set as the drying condition. Further alternatively, the drying condition setting device 71 may use data table 77 storing the relationship of target drying change amount ΔST and drying temperature T set as the drying condition. In other words, as long as drying temperature T is eventually calculated in accordance with obtained specific surface area Sd as the drying condition, calculation using a mathematical expression does not have to be performed before the drying condition setting device 71 refers to the data table 77.
The drying condition setting device 71 holds in advance the mathematical expression indicating the relationship between change amount ΔS of electrode plate specific surface area Se resulting from drying the electrode mixture 50 and drying temperature T. In this case, the mathematical expression does not have to be a linear approximate expression such as “y=ax−b”. Also, as described in the above example, such a mathematical expression may be used to calculate drying temperature T in accordance with obtained specific surface area Sd without the data table 77.
In the above embodiment, drying temperature T is set in accordance with obtained specific surface area Sd as the drying condition of the electrode mixture 50 to adjust post-drying electrode plate specific surface area Se2. However, there is no limit to such a configuration. A drying condition other than drying temperature T may be changed to adjust post-drying electrode plate specific surface area Se2.
As shown in
As shown in
Therefore, when drying the electrode mixture 50, drying time t may be set to become longer as obtained specific surface area Sd becomes smaller. Even such a configuration readily adjusts post-drying electrode plate specific surface area Se2. This reduces variations of electrode plate specific surface area Se and improves uniformity of the battery performance.
Also, as shown in
In an example, the data table 77C may correlate difference δ of obtained specific surface area Sd and standard specific surface area Sc, target drying change amount ΔST, and drying time t set as the drying condition. Alternatively, the data table 77C may correlate difference δ of obtained specific surface area Sd and standard specific surface area Sc and drying time t set as the drying condition. Then, the data table 77C may correlate target drying change amount ΔST and drying time t set as the drying condition.
In other words, as long as drying time t is calculated in accordance with obtained specific surface area Sd as the drying condition, calculation using a mathematical expression does not have to be performed before the drying condition setting device 71C refers to the data table 77C. Instead of the data table 77C, the drying condition setting device 71C may hold an approximate expression indicating the relationship between change amount ΔS of electrode plate specific surface area Se resulting from drying the electrode mixture 50 and drying time t.
As shown in
In the above embodiment, a method for calculating drying temperature T in accordance with obtained specific surface area Sd so as to correct difference δ of obtained specific surface area Sd and standard specific surface area Sc is described using an example in which obtained specific surface area Sd is less than standard specific surface area Sc. However, there is no limit to such a configuration, and drying temperature T may be calculated to correct difference δ of obtained specific surface area Sd and standard specific surface area Sc in the same manner when obtained specific surface area Sd is greater than standard specific surface area Sc.
In the above embodiment, drying temperature T can be calculated in accordance with obtained specific surface area Sd that is greater than standard specific surface area Sc through the same procedure within a range where the approximate expression is satisfied even if drying temperature T is in a temperature range that is lower than the standard value of “175° C.” (refer to
The limit of adjustment in electrode plate specific surface area Se by changing the setting of drying temperature T based on the migration effect, which occurs when electrode mixture 50 is dried, corresponds to the range over which electrode plate specific surface area Se increases when the electrode mixture 50 is dried (refer to
Further, in the above embodiment, the relationship between change amount ΔS of electrode plate specific surface area Se resulting from drying the electrode mixture 50 and drying temperature T may not satisfy the approximate expression in a region where target drying change amount ΔST is near the adjustment limit. However, even in such a case, experiments, simulations, and the like may be conducted in advance to obtain the relationship between change amount ΔS of electrode plate specific surface area Se when the electrode mixture 50 is dried and drying temperature T within a range of the adjustment limit including a region near the adjustment limit.
Specifically, in this case, experiments, simulations, and the like may be conducted in advance to prepare data table 77 and an approximate expression for the range of the adjustment limit including a region near the adjustment limit. The approximate expression in this case may not be a linear approximate equation such as “y=ax−b”. Further, the data table 77 does not have to include a linear relationship of obtained specific surface area Sd and the set drying condition. Such a configuration widens the range that appropriately adjusts post-drying electrode plate specific surface area Se2.
The limit of adjustment in electrode plate specific surface area Se by changing the setting of the drying condition, that is, the lower limit of target drying change amount ΔST, corresponds to the specification of the manufactured electrode sheet 35. Specifically, the adjustment limit is not necessarily equal to “−0.1”, which is the lower limit of target drying change amount ΔST in the above embodiment. Thus, even when obtained specific surface area Sd is greater than standard specific surface area Sc, difference δ of obtained specific surface area Sd and standard specific surface area Sc may be corrected throughout the entire range of permissible tolerance α within the limit of adjustment by changing the setting of the drying condition.
In the above embodiment, when drying the electrode mixture 50, drying temperature T is set in accordance with obtained specific surface area Sd based on change amount ΔS of electrode plate specific surface area Se that varies in accordance with the drying condition so as to correct difference δ of obtained specific surface area Sd and standard specific surface area Sc. However, there is no limit to such a configuration. The drying temperature T set in accordance with obtained specific surface area Sd does not have to completely correct difference δ of obtained specific surface area Sd and standard specific surface area Sc. In other words, the degree of correction is not limited as long as variations of electrode plate specific surface area Se are reduced by adjusting post-drying electrode plate specific surface area Se2. Further, standard specific surface area Sc does not have to be specified.
In the above embodiment, specific surface area S of the electrode active material 55 is measured by a BET method that uses nitrogen as the adsorption gas. However, there is no limit to such a configuration, and the adsorption gas does not have to be nitrogen. Furthermore, specific surface area S of the electrode active material 55 does not have to be a BET specific surface area and may be a value measured by another method.
In the above embodiment, the drying condition is set in accordance with obtained specific surface area Sd of the electrode active material 55 during manufacture of the electrode sheet 35N of the negative electrode 4. However, there is no limit to such a configuration. The drying condition may be set in accordance with obtained specific surface area Sd during manufacture of the electrode sheet 35P of the positive electrode 3.
In the above embodiment, the electrode body 10 of the rechargeable battery 1 is formed by rolling the stack of the positive and negative electrode sheets 35P and 35N arranged with the separator 5 held in between. However, there is no limit to such a structure, and the rechargeable battery 1 may include the electrode body 10 having a stack of flat layers.
Further, in the above embodiment, the method for manufacturing the rechargeable battery of the present disclosure is applied to the rechargeable battery 1 including the structure of a lithium-ion rechargeable battery. However, there is no limit to such a configuration, and the method for manufacturing the rechargeable battery of the present disclosure may be applied to a rechargeable battery 1 that is not a lithium-ion rechargeable battery.
The shapes of the positive electrode terminal 38P and the negative electrode terminal 38N are not limited to those shown in
Technical concepts that can be understood from the above embodiment and the modified examples will now be described.
Various changes in form and details may be made to the examples above without departing from the spirit and scope of the claims and their equivalents. The examples are for the sake of description only, and not for purposes of limitation. Descriptions of features in each example are to be considered as being applicable to similar features or aspects in other examples. Suitable results may be achieved if sequences are performed in a different order, and/or if components in a described system, architecture, device, or circuit are combined differently, and/or replaced or supplemented by other components or their equivalents. The scope of the disclosure is not defined by the detailed description, but by the claims and their equivalents. All variations within the scope of the claims and their equivalents are included in the disclosure.
Number | Date | Country | Kind |
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2022-080750 | May 2022 | JP | national |