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JP7765442B2 - Method for evaluating electrode distance in non-aqueous electrolyte secondary battery and method for manufacturing non-aqueous electrolyte secondary battery - Google Patents
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JP7765442B2 - Method for evaluating electrode distance in non-aqueous electrolyte secondary battery and method for manufacturing non-aqueous electrolyte secondary battery - Google Patents

Method for evaluating electrode distance in non-aqueous electrolyte secondary battery and method for manufacturing non-aqueous electrolyte secondary battery

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JP7765442B2
JP7765442B2 JP2023166096A JP2023166096A JP7765442B2 JP 7765442 B2 JP7765442 B2 JP 7765442B2 JP 2023166096 A JP2023166096 A JP 2023166096A JP 2023166096 A JP2023166096 A JP 2023166096A JP 7765442 B2 JP7765442 B2 JP 7765442B2
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崇礼 副島
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Prime Planet Energy and Solutions Inc
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Description

本開示技術は、非水電解液二次電池の電極体における極間距離の評価方法及び当該極間距離の評価方法を用いて製造する非水電解液二次電池の製造方法に関する。 The disclosed technology relates to a method for evaluating the inter-electrode distance in an electrode assembly of a non-aqueous electrolyte secondary battery and a method for manufacturing a non-aqueous electrolyte secondary battery using the inter-electrode distance evaluation method.

例えば、特許文献1には、正極、負極、およびセパレータを有する電極体と、非水電解液と、前記電極体および前記非水電解液を収容する電池ケースと、を備えるリチウムイオン二次電池が開示されている。このようなリチウムイオン二次電池では、大電流で長時間充電した場合等に、負極側に金属リチウム(デンドライト)が析出し、電極体の短絡や劣化に繋がる恐れがあることが知られている。 For example, Patent Document 1 discloses a lithium-ion secondary battery comprising an electrode assembly having a positive electrode, a negative electrode, and a separator, a non-aqueous electrolyte, and a battery case that houses the electrode assembly and the non-aqueous electrolyte. It is known that when such lithium-ion secondary batteries are charged with a large current for a long period of time, metallic lithium (dendrites) may precipitate on the negative electrode, potentially leading to short-circuiting or deterioration of the electrode assembly.

上記金属リチウムの析出が生じる要因は、種々考えられるが、電極体の極間距離が部分的に広いことが、その要因の一つであることが分かっている。すなわち、極間距離が部分的に広いと、その極間距離の変化点で局所的に過充電状態が生じ、負極付近に過剰に集まったリチウムイオンが負極側の電子を受取り、金属リチウムとして負極側に析出しやすくなる。 There are various possible reasons why metallic lithium is deposited, but it is known that one of the reasons is that the inter-electrode distance of the electrode assembly is partially wide. In other words, when the inter-electrode distance is partially wide, a localized overcharge state occurs at the point where the inter-electrode distance changes, and excess lithium ions that gather near the negative electrode accept electrons from the negative electrode, making it more likely for metallic lithium to deposit on the negative electrode.

特開2019-67699号公報JP 2019-67699 A

しかしながら、この金属リチウムの析出に関与する電極体の極間距離は、例えばCT(コンピュータ断層撮影)画像解析によっても測定可能であるが、複数の断面を測定する必要があるので、測定時間及び解析時間が長くなり、生産性が求められる製造工程において全数測定が困難であるという問題があった。また、電極体の極間距離は、例えば金属箔の状態や活物質層の塗工状態等によって、電極内部においてバラツキが生じ得るので、外観からの測定が難しいという問題があった。なお、デンドライト析出の問題は、リチウムイオン二次電池に限らず、ナトリウムイオン二次電池等を含む非水電解液二次電池に共通する問題であった。 However, while the inter-electrode distance of the electrode body involved in this metallic lithium deposition can be measured using, for example, CT (computed tomography) image analysis, the need to measure multiple cross sections increases the measurement and analysis time, making it difficult to measure all electrodes in manufacturing processes where productivity is essential. Furthermore, the inter-electrode distance of the electrode body can vary within the electrode depending on, for example, the condition of the metal foil or the coating condition of the active material layer, making it difficult to measure from the outside. The problem of dendrite deposition is not limited to lithium-ion secondary batteries, but is a common issue with non-aqueous electrolyte secondary batteries, including sodium-ion secondary batteries.

本開示技術は、かかる問題に鑑みてなされたものであって、リチウムイオン二次電池等を含む非水電解液二次電池の製造段階において、電極体の極間距離の適否を短時間で簡単に評価し得る非水電解液二次電池の極間距離の評価方法、及び当該極間距離の評価方法を用いた非水電解液二次電池の製造方法を提供することを課題とする。 The disclosed technology was developed in consideration of these problems, and aims to provide a method for evaluating the inter-electrode distance of a non-aqueous electrolyte secondary battery, which can quickly and easily evaluate the suitability of the inter-electrode distance of an electrode assembly during the manufacturing stage of non-aqueous electrolyte secondary batteries, including lithium-ion secondary batteries, and a method for manufacturing a non-aqueous electrolyte secondary battery using this inter-electrode distance evaluation method.

(1)上記課題を解決するための本開示技術の一態様は、正極体と負極体とがセパレータを挟んで積層された電極体と、前記電極体の極間に浸透した非水電解液と、前記非水電解液であって前記電極体の極間に浸透していない余剰電解液と、をケース内に収容した非水電解液二次電池の製造段階において、
前記ケース内に前記余剰電解液が残るように前記非水電解液を注入する電解液注入工程と、前記ケース内の前記余剰電解液を前記電極体の極間に強制的に浸透させる電解液強制浸透工程と、前記電解液注入工程後で、前記電解液強制浸透工程前に、前記ケース内の前記余剰電解液の液量を計測する第1液量計測工程と、前記電解液強制浸透工程後に、前記ケース内の前記余剰電解液の液量を計測する第2液量計測工程と、前記第1液量計測工程で計測した液量から前記第2液量計測工程で計測した液量を差し引いた前記余剰電解液の液変化量が、所定の基準値以下の場合に、前記電極体の極間距離が適正と評価する評価工程と、を備えた非水電解液二次電池の極間距離の評価方法である。
(1) One aspect of the disclosed technique for solving the above problem is to provide a non-aqueous electrolyte secondary battery in a manufacturing stage, in which an electrode assembly in which a positive electrode body and a negative electrode body are stacked with a separator sandwiched therebetween, a non-aqueous electrolyte solution that has permeated between the electrodes of the electrode assembly, and an excess electrolyte solution of the non-aqueous electrolyte solution that has not permeated between the electrodes of the electrode assembly are housed in a case,
a forced electrolyte penetration step of forcibly penetrating the excess electrolyte in the case between the electrodes of the electrode body; a first liquid volume measurement step of measuring the liquid volume of the excess electrolyte in the case after the electrolyte injection step and before the forced electrolyte penetration step; a second liquid volume measurement step of measuring the liquid volume of the excess electrolyte in the case after the forced electrolyte penetration step; and an evaluation step of evaluating the inter-electrode distance of the electrode body as appropriate when a change in the liquid volume of the excess electrolyte, calculated by subtracting the liquid volume measured in the second liquid volume measurement step from the liquid volume measured in the first liquid volume measurement step, is equal to or less than a predetermined reference value.

(2)(1)に記載された非水電解液二次電池の極間距離の評価方法において、前記第2液量計測工程は、前記電解液強制浸透工程後であって、前記非水電解液二次電池に対する常温下で複数回充放電を行うコンディショニング工程及び高温下に所定時間放置するエージング工程の後に行うことが好ましい。 (2) In the method for evaluating the inter-electrode distance of a nonaqueous electrolyte secondary battery described in (1), the second liquid volume measurement step is preferably performed after the forced electrolyte penetration step, and after a conditioning step in which the nonaqueous electrolyte secondary battery is charged and discharged multiple times at room temperature and an aging step in which the battery is left at a high temperature for a predetermined period of time.

(3)上記課題を解決するための本開示技術の他の態様は、(1)又は(2)に記載された非水電解液二次電池の極間距離の評価方法を用いた非水電解液二次電池の製造方法である。 (3) Another aspect of the disclosed technology for solving the above problem is a method for manufacturing a nonaqueous electrolyte secondary battery using the method for evaluating the inter-electrode distance of a nonaqueous electrolyte secondary battery described in (1) or (2).

本実施形態の一態様に係る非水電解液二次電池の概略断面図である。1 is a schematic cross-sectional view of a nonaqueous electrolyte secondary battery according to one aspect of the present embodiment. 図1に示す電極体の正極体と負極体とを、セパレータを挟んで積層して巻回する巻回途中の状態を表す模式的斜視図である。2 is a schematic perspective view showing a state in the middle of winding the positive electrode body and the negative electrode body of the electrode assembly shown in FIG. 1, with a separator sandwiched therebetween. FIG. 図1に示すA部の本実施例における電極体の積層状態を表す模式的断面図である。2 is a schematic cross-sectional view showing a stacked state of the electrode body in the present embodiment of the part A shown in FIG. 1. FIG. 図1に示すA部の比較例における電極体の積層状態を表す模式的断面図である。2 is a schematic cross-sectional view showing a stacked state of an electrode body in a comparative example of part A shown in FIG. 1 . 図1に示す非水電解液二次電池のケース内の余剰電解液の液量を計測する計測装置及び極間距離の評価装置の概略断面図である。2 is a schematic cross-sectional view of a measuring device for measuring the amount of excess electrolyte in the case of the nonaqueous electrolyte secondary battery shown in FIG. 1 and an evaluation device for the interelectrode distance. 図5に示す計測装置の変形例であって、非水電解液二次電池を傾斜した状態で余剰電解液の液量を計測する場合の概略断面図である。FIG. 6 is a schematic cross-sectional view showing a modified example of the measuring device shown in FIG. 5, in which the amount of excess electrolyte is measured while the nonaqueous electrolyte secondary battery is tilted. 図1に示す非水電解液二次電池の極間距離の評価方法における手順を表すフローチャート図である。FIG. 2 is a flowchart showing the steps of a method for evaluating the inter-electrode distance of the nonaqueous electrolyte secondary battery shown in FIG. 1 . 図1に示す非水電解液二次電池の製造方法における手順を表すフローチャート図である。FIG. 2 is a flowchart showing steps in a method for manufacturing the nonaqueous electrolyte secondary battery shown in FIG. 1 .

<本非水電解液二次電池の説明>
次に、上記開示技術の実施形態に係る極間距離の評価方法の対象となる非水電解液二次電池の構成について、図面を参照しつつ詳細に説明する。図1に、本実施形態の一態様に係る非水電解液二次電池の概略断面図を示す。図2に、図1に示す電極体の正極体と負極体とを、セパレータを挟んで積層して巻回する巻回途中の状態を表す模式的斜視図を示す。図3に、図1に示すA部の本実施例における電極体の積層状態を表す模式的断面図を示す。図4に、図1に示すA部の比較例における電極体の積層状態を表す模式的断面図を示す。
<Description of the Non-Aqueous Electrolyte Secondary Battery>
Next, the configuration of a nonaqueous electrolyte secondary battery that is the subject of the inter-electrode distance evaluation method according to the embodiment of the disclosed technology will be described in detail with reference to the drawings. Fig. 1 shows a schematic cross-sectional view of a nonaqueous electrolyte secondary battery according to one aspect of this embodiment. Fig. 2 shows a schematic perspective view of the electrode assembly shown in Fig. 1 in the middle of being stacked and wound with a separator sandwiched between the positive electrode body and the negative electrode body. Fig. 3 shows a schematic cross-sectional view of the stacked state of the electrode assembly in this example at part A shown in Fig. 1. Fig. 4 shows a schematic cross-sectional view of the stacked state of the electrode assembly in a comparative example at part A shown in Fig. 1.

本非水電解液二次電池10の一態様(本実施例)は、図1~図3に示すように、正極体11と負極体12とがセパレータ13を挟んで積層された電極体1と、電極体1の極間DKに浸透した非水電解液2と、同じ非水電解液2であって電極体1の極間DKに浸透していない余剰電解液2Yと、をケース3内に収容した非水電解液二次電池10(10B)である。この非水電解液二次電池10(10B)は、その種類(例えば、リチウムイオン二次電池、ナトリウム二次電池等)を限定するものではない。 As shown in FIGS. 1 to 3, one embodiment (this embodiment) of the nonaqueous electrolyte secondary battery 10 is a nonaqueous electrolyte secondary battery 10 (10B) that contains, in a case 3, an electrode assembly 1 in which a cathode body 11 and an anode body 12 are stacked with a separator 13 sandwiched therebetween, a nonaqueous electrolyte 2 that has permeated the inter-electrode DK of the electrode assembly 1, and surplus electrolyte 2Y of the same nonaqueous electrolyte 2 that has not permeated the inter-electrode DK of the electrode assembly 1. There are no limitations on the type of this nonaqueous electrolyte secondary battery 10 (10B) (e.g., lithium-ion secondary battery, sodium secondary battery, etc.).

図1に示すように、ケース3は、例えば、アルミ合金製であって、開口部313を有するケース本体31と、開口部313を封口するケース蓋体32とで構成されている。ここでは、ケース本体31は、長方形状の底板311と、底板311の外周縁から垂直状に起立する側板312とを有し、一体成形で形成されている。ケース蓋体32は、長方形状の板体に形成され、その中央付近に電解液2を注入する注入口321と安全弁322とが形成されている。なお、ケース本体31とケース蓋体32は、上記形状に限る必要はなく、各種形状にしても良い。 As shown in FIG. 1, the case 3 is made of, for example, an aluminum alloy and is composed of a case body 31 having an opening 313, and a case lid 32 that seals the opening 313. Here, the case body 31 has a rectangular bottom plate 311 and side plates 312 that stand vertically from the outer edge of the bottom plate 311, and is formed as a single unit. The case lid 32 is formed as a rectangular plate, and is provided with an inlet 321 for injecting the electrolyte 2 and a safety valve 322 near its center. Note that the case body 31 and case lid 32 are not limited to the shapes described above and may have various other shapes.

また、ケース蓋体32の長手方向の両端部には、端子挿通孔323が形成され、当該端子挿通孔323に嵌装された絶縁部材5を介して正負の集電端子4(41、42)が結合されている。正極集電端子41の上端部には、正極の外部接続部411が形成され、その下端部には、電極体1の正極体11と電気的に接続される内部接続部412が形成されている。負極集電端子42の上端部には、負極の外部接続部421が形成され、その下端部には、電極体1の負極体12と電気的に接続される内部接続部422が形成されている。 In addition, terminal insertion holes 323 are formed at both longitudinal ends of the case lid 32, and positive and negative current collector terminals 4 (41, 42) are connected via insulating members 5 fitted into the terminal insertion holes 323. A positive electrode external connection portion 411 is formed at the upper end of the positive current collector terminal 41, and an internal connection portion 412 that is electrically connected to the positive electrode body 11 of the electrode body 1 is formed at its lower end. A negative electrode external connection portion 421 is formed at the upper end of the negative current collector terminal 42, and an internal connection portion 422 that is electrically connected to the negative electrode body 12 of the electrode body 1 is formed at its lower end.

また、図2、図3に示すように、電極体1は、正極体11と負極体12とがセパレータ13を挟んで積層され、偏平状に圧着した状態で巻回されている。電極体1は、巻回型の電極体に限らず、例えば、シート積層型の電極体でも良い。正極体11は、集電箔(例えば、アルミ箔)111の一端部(非塗工部)を除き、その両面に正極活物質層112が略一定の厚さで塗工されている。負極体12は、集電箔(例えば、銅箔)121の一端部(非塗工部)を除き、その両面に負極活物質層122が略一定の厚さで塗工されている。なお、正極体11の非塗工部は、正極集電端子41の内部接続部412と接続され、負極体12の非塗工部は、負極集電端子42の内部接続部422と接続されている。 2 and 3, the electrode body 1 is formed by stacking a positive electrode body 11 and a negative electrode body 12 with a separator 13 sandwiched therebetween and rolling them in a flat, pressure-bonded state. The electrode body 1 is not limited to a wound-type electrode body, but may be, for example, a sheet-laminated electrode body. The positive electrode body 11 has a current collector foil (e.g., aluminum foil) 111 coated with a positive electrode active material layer 112 of approximately uniform thickness on both sides thereof, except for one end (uncoated portion) of the current collector foil (e.g., copper foil). The negative electrode body 12 has a current collector foil (e.g., copper foil) 121 coated with a negative electrode active material layer 122 of approximately uniform thickness on both sides thereof, except for one end (uncoated portion) of the current collector foil. The uncoated portion of the positive electrode body 11 is connected to the internal connection portion 412 of the positive electrode collector terminal 41, and the uncoated portion of the negative electrode body 12 is connected to the internal connection portion 422 of the negative electrode collector terminal 42.

ここで、電極体1の極間距離DLは、正極体11の集電箔111と負極体12の集電箔121との離間距離を意味し、図3は、正極体11とセパレータ13と負極体12とが適正な極間距離DL1で積層された状態を示す。そして、電解液2は、正極活物質層112とセパレータ13と負極活物質層122との僅かな隙間、各活物質層112,122の活物質同士の微細隙間、及びセパレータ13の細孔に浸透されている。なお、セパレータ13は、図示しない電荷担体(例えば、リチウムイオン等)が通過可能に塗布された接着材を介して正極活物質層112及び負極活物質層122と接着されている。 Here, the inter-electrode distance DL of the electrode body 1 refers to the distance between the current collector foil 111 of the positive electrode body 11 and the current collector foil 121 of the negative electrode body 12. Figure 3 shows the positive electrode body 11, separator 13, and negative electrode body 12 stacked at the appropriate inter-electrode distance DL1. The electrolyte 2 permeates the small gaps between the positive electrode active material layer 112, separator 13, and negative electrode active material layer 122, the minute gaps between the active materials of each active material layer 112, 122, and the pores of the separator 13. The separator 13 is adhered to the positive electrode active material layer 112 and negative electrode active material layer 122 via an adhesive applied to allow charge carriers (e.g., lithium ions, etc.) to pass through (not shown).

図3に示すように、正極体11とセパレータ13と負極体12とが適正な極間距離DL1で積層されている場合、正極体11と負極体12との間の内部抵抗が略一定となり、充放電時に流れる電流が均一化されて、局部的な過充電が生じにくい。そのため、非水電解液二次電池(例えば、リチウムイオン二次電池)において、デンドライト(例えば、金属リチウム)が負極体12の表面に析出しにくい。 As shown in Figure 3, when the positive electrode body 11, separator 13, and negative electrode body 12 are stacked with the appropriate inter-electrode distance DL1, the internal resistance between the positive electrode body 11 and the negative electrode body 12 becomes approximately constant, the current flowing during charging and discharging is uniform, and localized overcharging is less likely to occur. Therefore, in non-aqueous electrolyte secondary batteries (e.g., lithium ion secondary batteries), dendrites (e.g., metallic lithium) are less likely to precipitate on the surface of the negative electrode body 12.

これに対して、図4に示す比較例の非水電解液二次電池10Bの電極体1Bのように、正極体11とセパレータ13と負極体12Bとが部分的に広い極間距離DL2で積層されている場合、広い極間距離DL2の領域では、正極体11と負極体12Bとの間の内部抵抗が高くなり、充放電時に流れる電流が減少する。一方で、極間距離DL2の距離変化点の凸領域HPにおいて、局部的な過充電が生じやすく、デンドライト(例えば、金属リチウム)が負極体12Bの凸領域HPに析出しやすい。この部分的に広い極間距離DL2の領域は、電極体1Bの負極集電箔121Bの変形、負極活物質層122Bの塗工厚さのバラツキ等によって、電極体1Bの製造段階で生じ得る。したがって、デンドライト(例えば、金属リチウム)の析出耐性の高い高品質の非水電解液二次電池10を提供するためには、非水電解液二次電池10の製造段階で、相対的に広い極間距離DLの領域が多いか否かを評価することが重要となる。 In contrast, when the cathode body 11, separator 13, and anode body 12B are stacked with a partially wide inter-electrode distance DL2, as in the electrode body 1B of the comparative nonaqueous electrolyte secondary battery 10B shown in Figure 4, the internal resistance between the cathode body 11 and the anode body 12B increases in the region of the wide inter-electrode distance DL2, reducing the current flow during charging and discharging. Meanwhile, localized overcharging is likely to occur in the convex region HP where the inter-electrode distance DL2 changes, and dendrites (e.g., metallic lithium) are likely to precipitate in the convex region HP of the anode body 12B. This partially wide inter-electrode distance DL2 region can arise during the manufacturing process of the electrode body 1B due to deformation of the anode current collector foil 121B of the electrode body 1B, variations in the coating thickness of the anode active material layer 122B, and other factors. Therefore, in order to provide a high-quality nonaqueous electrolyte secondary battery 10 that is highly resistant to dendrite (e.g., metallic lithium) precipitation, it is important to evaluate whether there are many regions with a relatively wide inter-electrode distance DL during the manufacturing stage of the nonaqueous electrolyte secondary battery 10.

なお、非水電解液二次電池10、10Bは、その種類(例えば、リチウムイオン二次電池、ナトリウム二次電池等)を限定するものではないが、正極活物質層112とセパレータ13と負極活物質層122と電解液2は、非水電解液二次電池10の種類に応じて異なり、それぞれ公知のものを用いることができる。 The nonaqueous electrolyte secondary batteries 10 and 10B are not limited to any particular type (e.g., lithium-ion secondary batteries, sodium secondary batteries, etc.), but the positive electrode active material layer 112, separator 13, negative electrode active material layer 122, and electrolyte 2 vary depending on the type of nonaqueous electrolyte secondary battery 10, and known materials can be used for each.

<本非水電解液二次電池の極間距離の評価方法>
以下に、非水電解液二次電池の製造段階において、上記デンドライト析出に関与する電極体の極間距離の適否を、短時間で簡単に評価し得る非水電解液二次電池の極間距離の評価方法を、図1~図7を参照しつつ説明する。図5に、図1に示す非水電解液二次電池のケース内の余剰電解液の液量を計測する計測装置及び極間距離の評価装置の概略断面図を示す。図6に、図5に示す計測装置の変形例であって、非水電解液二次電池を傾斜した状態で余剰電解液の液量を計測する場合の概略断面図を示す。図7に、図1に示す非水電解液二次電池の極間距離の評価方法における手順を表すフローチャート図を示す。
<Method for Evaluating the Distance Between Electrodes of the Present Non-Aqueous Electrolyte Secondary Battery>
A method for evaluating the inter-electrode distance of a non-aqueous electrolyte secondary battery, which can quickly and easily evaluate the suitability of the inter-electrode distance of an electrode assembly involved in the dendrite deposition during the manufacturing stage of the non-aqueous electrolyte secondary battery, will be described below with reference to FIGS. 1 to 7. FIG. 5 shows a schematic cross-sectional view of a measuring device for measuring the amount of excess electrolyte in the case of the non-aqueous electrolyte secondary battery shown in FIG. 1 and an inter-electrode distance evaluating device. FIG. 6 shows a schematic cross-sectional view of a modified version of the measuring device shown in FIG. 5, in which the amount of excess electrolyte is measured with the non-aqueous electrolyte secondary battery in an inclined state. FIG. 7 shows a flowchart illustrating the steps in the method for evaluating the inter-electrode distance of the non-aqueous electrolyte secondary battery shown in FIG. 1.

図1~図7に示すように、本非水電解液二次電池10(10B)の極間距離DLの評価方法SSは、正極体11と負極体12とがセパレータ13を挟んで積層された電極体1と、電極体1の極間DKに浸透した非水電解液2と、非水電解液2であって電極体1の極間DKに浸透していない余剰電解液2Yと、をケース3内に収容した非水電解液二次電池10の製造段階において、下記工程を備えている。 As shown in Figures 1 to 7, the evaluation method SS for the inter-electrode distance DL of the nonaqueous electrolyte secondary battery 10 (10B) includes the following steps during the manufacturing stage of the nonaqueous electrolyte secondary battery 10, which contains, in a case 3, an electrode assembly 1 in which a positive electrode body 11 and a negative electrode body 12 are stacked with a separator 13 sandwiched between them, nonaqueous electrolyte 2 that has permeated the inter-electrode DK of the electrode assembly 1, and excess electrolyte 2Y that is nonaqueous electrolyte 2 but has not permeated the inter-electrode DK of the electrode assembly 1.

すなわち、非水電解液二次電池10の極間距離DLの評価方法SSは、(a)ケース3内に余剰電解液2Yが残るように非水電解液2を注入する電解液注入工程S1と、(b)ケース3内の余剰電解液2Yを電極体1の極間DKに強制的に浸透させる電解液強制浸透工程S3と、(c)電解液注入工程S1後で、電解液強制浸透工程S3前に、ケース3内の余剰電解液2Yの液量L0を計測する第1液量計測工程S2と、(d)電解液強制浸透工程S3後に、ケース3内の余剰電解液2Yの液量L1を計測する第2液量計測工程S4と、(e)第1液量計測工程S2で計測した液量L0から第2液量計測工程S4で計測した液量L1を差し引いた余剰電解液2Yの液変化量ΔLが、所定の基準値KJ以下の場合に、電極体1の極間距離DLが適正と評価する評価工程S5と、を備えている。 That is, the evaluation method SS for the inter-electrode distance DL of the nonaqueous electrolyte secondary battery 10 includes: (a) an electrolyte injection step S1 in which nonaqueous electrolyte 2 is injected so that excess electrolyte 2Y remains in the case 3; (b) a forced electrolyte penetration step S3 in which the excess electrolyte 2Y in the case 3 is forced to penetrate into the inter-electrode distance DK of the electrode body 1; and (c) measuring the liquid volume L0 of the excess electrolyte 2Y in the case 3 after the electrolyte injection step S1 and before the forced electrolyte penetration step S3. The method includes (d) a first liquid volume measurement process S2, (e) a second liquid volume measurement process S4 for measuring the liquid volume L1 of the excess electrolyte 2Y in the case 3 after the electrolyte forced penetration process S3, and (f) an evaluation process S5 for evaluating the inter-electrode distance DL of the electrode body 1 as appropriate if the liquid volume change ΔL of the excess electrolyte 2Y, obtained by subtracting the liquid volume L1 measured in the second liquid volume measurement process S4 from the liquid volume L0 measured in the first liquid volume measurement process S2, is equal to or less than a predetermined reference value KJ.

(a)電解液注入工程S1では、図示しない電解液吐出ノズルを、ケース蓋体32の注入口321から、ケース3内に収納された電極体1の上端部とケース蓋体32との間に挿入し、当該電解液吐出ノズルから必要量の非水電解液2をケース3内に注入する。この段階では、注入した非水電解液2の内、一部は電極体1の外周側の極間DKに浸透するが、電極体1の内周側の極間DKには浸透しにくく、電極体1の極間DKに浸透しない余剰電解液2Yがケース3内に残っている。 (a) In the electrolyte injection process S1, an electrolyte discharge nozzle (not shown) is inserted through the injection port 321 of the case lid 32 between the upper end of the electrode body 1 housed in the case 3 and the case lid 32, and the required amount of nonaqueous electrolyte 2 is injected into the case 3 from the electrolyte discharge nozzle. At this stage, some of the injected nonaqueous electrolyte 2 penetrates into the inter-electrode DK on the outer periphery of the electrode body 1, but it does not penetrate easily into the inter-electrode DK on the inner periphery of the electrode body 1, and excess electrolyte 2Y that does not penetrate into the inter-electrode DK of the electrode body 1 remains in the case 3.

(b)電解液強制浸透工程S3では、ケース3内の余剰電解液2Yを電極体1の極間DKに強制的に浸透させる。このとき、ケース3内の余剰電解液2Yは、電極体1の内周側に広い極間距離DLの領域が多く存在するほど、多く減少する。したがって、ケース3内の余剰電解液2Yの液変化量ΔLが大きい程、電極体1の極間距離DLが内周側に広い領域が多く存在し、デンドライト(例えば、リチウム金属)析出耐性が低いことになる。なお、余剰電解液2Yを電極体1の極間DKに強制的に浸透させる方法は、特に限定されないが、例えば、ケース3の内圧を増減し、圧力差によって浸透させる方法、又はケース3を振動させて、慣性力によって浸透させる方法等が含まれる。 (b) In the forced electrolyte penetration step S3, excess electrolyte 2Y in the case 3 is forced to penetrate into the inter-electrode gap DK of the electrode body 1. At this time, the excess electrolyte 2Y in the case 3 decreases more as the number of regions with a wider inter-electrode distance DL increases on the inner circumferential side of the electrode body 1. Therefore, the greater the amount of solution change ΔL of the excess electrolyte 2Y in the case 3, the more regions with a wider inter-electrode distance DL exist on the inner circumferential side of the electrode body 1, and the lower the resistance to dendrite (e.g., lithium metal) precipitation. Note that the method for forcibly penetrating excess electrolyte 2Y into the inter-electrode gap DK of the electrode body 1 is not particularly limited, but includes, for example, a method of increasing or decreasing the internal pressure of the case 3 to cause penetration by pressure difference, or a method of vibrating the case 3 to cause penetration by inertial force.

(c)第1液量計測工程S2では、電解液注入工程S1後で、電解液強制浸透工程S3前に、ケース3内の余剰電解液2Yの液量L0を計測する。また、(d)第2液量計測工程S4では、電解液強制浸透工程S3後に、ケース3内の余剰電解液2Yの液量L1を計測する。この液量L0、L1の計測は、CT画像解析と異なり、非水電解液二次電池10の製造段階で、製造ラインのタクト時間(例えば、十数秒)に合うように、短時間で簡単に計測することができる。 (c) In the first liquid volume measurement step S2, the liquid volume L0 of the excess electrolyte 2Y in the case 3 is measured after the electrolyte injection step S1 and before the forced electrolyte penetration step S3. (d) In the second liquid volume measurement step S4, the liquid volume L1 of the excess electrolyte 2Y in the case 3 is measured after the forced electrolyte penetration step S3. Unlike CT image analysis, these liquid volumes L0 and L1 can be measured easily and quickly during the manufacturing stage of the nonaqueous electrolyte secondary battery 10 to fit the takt time (e.g., several tens of seconds) of the manufacturing line.

第1液量計測工程S2及び第2液量計測工程S4に用いる計測装置6は、例えば、図5に示すように、透視線照射装置61と、透視画像計測装置62と、計測する非水電解液二次電池10(10B)を載置するテーブル装置63と、を備えている。ここで、透視線照射装置61は、非水電解液二次電池10(10B)の内部を透視可能な透視線64を照射する装置(例えば、X線照射装置)である。透視画像計測装置62は、透視線64の透視画像に基づいて計測する、余剰電解液2Yのケース本体31の底板311に対する液面高さH1、H2等と、余剰電解液2Yの液面下に存在する電極体1の体積R1、R2と、から下記数式(1)、数式(2)によって、余剰電解液2Yの液量L0、L1を計測する装置である。
L0=H1×D1×D2-R1・・・・数式(1)
L1=H2×D1×D2-R2・・・・数式(2)
5, the measuring device 6 used in the first liquid volume measuring step S2 and the second liquid volume measuring step S4 includes, for example, a fluoroscopic line irradiating device 61, a fluoroscopic image measuring device 62, and a table device 63 on which the nonaqueous electrolyte secondary battery 10 (10B) to be measured is placed. Here, the fluoroscopic line irradiating device 61 is a device (e.g., an X-ray irradiating device) that irradiates a fluoroscopic line 64 that allows the interior of the nonaqueous electrolyte secondary battery 10 (10B) to be seen through. The fluoroscopic image measuring device 62 is a device that measures the liquid volumes L0 and L1 of the excess electrolyte 2Y using the liquid level heights H1, H2, etc. of the excess electrolyte 2Y relative to the bottom plate 311 of the case body 31, and the volumes R1 and R2 of the electrode body 1 present below the liquid level of the excess electrolyte 2Y, measured based on the fluoroscopic image of the fluoroscopic line 64, using the following formulas (1) and (2).
L0 = H1 x D1 x D2 - R1 Formula (1)
L1 = H2 x D1 x D2 - R2 Formula (2)

なお、D1は、ケース本体31の底板311の長手方向長さであり、D2は、ケース本体31の底板311の短手方向長さであり、R1は、第1液量計測工程S2で計測する余剰電解液2Yの液面下に存在する電極体1の体積であり、R2は、第2液量計測工程S4で計測する余剰電解液2Yの液面下に存在する電極体1の体積である。 Note that D1 is the longitudinal length of the bottom plate 311 of the case body 31, D2 is the lateral length of the bottom plate 311 of the case body 31, R1 is the volume of the electrode body 1 present below the liquid surface of the excess electrolyte 2Y measured in the first liquid volume measurement process S2, and R2 is the volume of the electrode body 1 present below the liquid surface of the excess electrolyte 2Y measured in the second liquid volume measurement process S4.

(e)評価工程S5では、第1液量計測工程S2で計測した液量L0から第2液量計測工程S4で計測した液量L1を差し引いた余剰電解液2Yの液変化量ΔLが、所定の基準値KJ以下の場合に、電極体1の極間距離DLが適正と評価する。この評価工程S5に用いる評価装置7は、計測装置6(透視画像計測装置62)と接続されている。評価装置7は、例えば、第1液量計測工程S2で計測した余剰電解液2Yの液量L0と、第2液量計測工程S4で計測した余剰電解液2Yの液量L1と、の差分(L0-L1)から余剰電解液2Yの液変化量ΔLを求める演算回路71と、所定の基準値KJを入力し、入力した基準値KJを記憶する入力・記憶回路72と、液変化量ΔLと基準値KJとを比較して電極体1の極間距離DLの適正、不適正を判定する判定回路73と、を備えている。 (e) In the evaluation step S5, if the liquid change amount ΔL of the excess electrolyte 2Y, calculated by subtracting the liquid volume L1 measured in the second liquid volume measurement step S4 from the liquid volume L0 measured in the first liquid volume measurement step S2, is less than or equal to a predetermined reference value KJ, the inter-electrode distance DL of the electrode body 1 is evaluated as appropriate. The evaluation device 7 used in this evaluation step S5 is connected to the measurement device 6 (fluoroscopic image measurement device 62). The evaluation device 7 includes, for example, a calculation circuit 71 that calculates the amount of change in the liquid level ΔL of the excess electrolyte 2Y from the difference (L0-L1) between the liquid level L0 of the excess electrolyte 2Y measured in the first liquid level measurement process S2 and the liquid level L1 of the excess electrolyte 2Y measured in the second liquid level measurement process S4; an input/storage circuit 72 that inputs a predetermined reference value KJ and stores the input reference value KJ; and a judgment circuit 73 that compares the amount of change in the liquid level ΔL with the reference value KJ to judge whether the inter-electrode distance DL of the electrode body 1 is appropriate.

なお、基準値KJは、非水電解液二次電池10の種類、形態、電池容量等に応じて、デンドライト(例えば、リチウム金属)析出耐性が良好となる液変化量の値を設定する。例えば、後述するコンディショニング工程S6後の放電容量に対する、ハイレート充放電試験後の放電容量の比率(容量維持率)が90%以上である場合に、デンドライト(例えば、リチウム金属)析出耐性は良好であることが分かっている。したがって、例えば、上記容量維持率が90%以上となる場合の液変化量ΔLの値を基準値KJとして、設定できる。 The reference value KJ is set to a value of the amount of solution change that provides good resistance to dendrite (e.g., lithium metal) precipitation, depending on the type, form, battery capacity, etc. of the nonaqueous electrolyte secondary battery 10. For example, it is known that good resistance to dendrite (e.g., lithium metal) precipitation is achieved when the ratio (capacity retention rate) of the discharge capacity after a high-rate charge-discharge test to the discharge capacity after the conditioning step S6 described below is 90% or higher. Therefore, for example, the value of the amount of solution change ΔL when the capacity retention rate is 90% or higher can be set as the reference value KJ.

また、ケース3内の余剰電解液2Yの液量が少ない場合、図6に示すように、非水電解液二次電池10(10B)の余剰電解液2Yが1つのケース角部314に集まるように、ケース3を傾斜した状態で余剰電解液2Yの液量を計測することが、好ましい。この場合、ケース3の底板311を載置するテーブル装置63Bの載置面を、上方へV字状に開く傾斜面(例えば、傾斜角θ=45°)として形成する。そして、当該傾斜面にケース3の底板311及び側板312を載置した状態で、図5に示す透視線照射装置61が、図面の法線方向から透視線64を照射し、透視画像計測装置62が透視線64の透視画像に基づいて計測する。この場合、下記数式(3)、数式(4)によって、余剰電解液2Yの液量L0、L1を正確に計測することができる。
L0=1/2×H1×W1×D2-T1・・・・数式(3)
L1=1/2×H2×W2×D2-T2・・・・数式(4)
Furthermore, when the amount of excess electrolyte 2Y in the case 3 is small, it is preferable to measure the amount of excess electrolyte 2Y while tilting the case 3 so that the excess electrolyte 2Y of the nonaqueous electrolyte secondary battery 10 (10B) gathers at one case corner 314, as shown in FIG. 6 . In this case, the mounting surface of a table device 63B on which the bottom plate 311 of the case 3 is placed is formed as an inclined surface that opens upward in a V-shape (e.g., inclination angle θ = 45°). Then, with the bottom plate 311 and side plates 312 of the case 3 placed on this inclined surface, a fluoroscopic line irradiation device 61 shown in FIG. 5 irradiates a fluoroscopic line 64 from the normal direction of the drawing, and a fluoroscopic image measurement device 62 performs measurement based on a fluoroscopic image of the fluoroscopic line 64. In this case, the amounts L0 and L1 of the excess electrolyte 2Y can be accurately measured using the following formulas (3) and (4).
L0 = 1/2 × H1 × W1 × D2 - T1 ... Formula (3)
L1 = 1/2 × H2 × W2 × D2 - T2 ... Formula (4)

なお、W1は、第1液量計測工程S2で計測する余剰電解液2Yの液面長さであり、W2は、第2液量計測工程S4で計測する余剰電解液2Yの液面長さであり、T1は、第1液量計測工程S2で計測する余剰電解液2Yの液面下に存在する電極体1の体積であり、T2は、第2液量計測工程S4で計測する余剰電解液2Yの液面下に存在する電極体1の体積である。また、D2は、ケース本体31の底板311の短手方向長さである。 W1 is the liquid surface length of the excess electrolyte 2Y measured in the first liquid volume measurement process S2, W2 is the liquid surface length of the excess electrolyte 2Y measured in the second liquid volume measurement process S4, T1 is the volume of the electrode body 1 present below the liquid surface of the excess electrolyte 2Y measured in the first liquid volume measurement process S2, and T2 is the volume of the electrode body 1 present below the liquid surface of the excess electrolyte 2Y measured in the second liquid volume measurement process S4. Also, D2 is the short-side length of the bottom plate 311 of the case body 31.

また、図7に示すように、本非水電解液二次電池10の極間距離DLの評価方法SSにおいて、第2液量計測工程S4は、電解液強制浸透工程S3後であって、非水電解液二次電池10に対する常温下で複数回充放電を行うコンディショニング工程S6及び高温下に所定時間放置するエージング工程S7の後に行うことが、好ましい。コンディショニング工程S6では、常温下で複数回充放電を繰り返すことによって、負極体12の表面近傍に電解液2に由来する保護被膜12H(図3参照)を形成できる。また、エージング工程S7では、高温下に所定時間放置し、金属異物の溶解や保護被膜12Hの安定化を行うことができる。この場合、コンディショニング工程S6及びエージング工程S7にて生じる電極体1の膨張収縮及び保護被膜12Hの形成等によって、ケース3内の余剰電解液2Yが僅かに減少するため、より正確な余剰電解液2Yの液変化量ΔLに基づいて、電極体1の極間距離DLの適正、不適正を判定できる。 As shown in Figure 7, in the evaluation method SS for the interelectrode distance DL of the nonaqueous electrolyte secondary battery 10, the second liquid volume measurement step S4 is preferably performed after the forced electrolyte penetration step S3, and after the conditioning step S6 in which the nonaqueous electrolyte secondary battery 10 is charged and discharged multiple times at room temperature and the aging step S7 in which the battery is left at a high temperature for a predetermined period of time. In the conditioning step S6, a protective coating 12H (see Figure 3) derived from the electrolyte 2 can be formed near the surface of the negative electrode body 12 by repeatedly charging and discharging the battery at room temperature multiple times. In the aging step S7, the battery is left at a high temperature for a predetermined period of time, allowing for the dissolution of metallic foreign matter and the stabilization of the protective coating 12H. In this case, the excess electrolyte 2Y in the case 3 decreases slightly due to the expansion and contraction of the electrode body 1 and the formation of the protective coating 12H that occur during the conditioning step S6 and the aging step S7. Therefore, the appropriateness of the inter-electrode distance DL of the electrode body 1 can be determined more accurately based on the amount of change ΔL in the excess electrolyte 2Y.

<極間距離の評価方法を用いた非水電解液二次電池の製造方法>
次に、上述した極間距離の評価方法を用いた非水電解液二次電池の製造方法について、図8を参照して説明する。図8に、図1に示す非水電解液二次電池の製造方法における手順を表すフローチャート図を示す。
<Method for manufacturing a non-aqueous electrolyte secondary battery using an interelectrode distance evaluation method>
Next, a method for manufacturing a nonaqueous electrolyte secondary battery using the above-described method for evaluating the interelectrode distance will be described with reference to Fig. 8. Fig. 8 is a flowchart showing the steps in the method for manufacturing the nonaqueous electrolyte secondary battery shown in Fig. 1.

本非水電解液二次電池10の製造方法は、上述した非水電解液二次電池10の極間距離DLの評価方法SSを用いている。すなわち、本非水電解液二次電池10の製造方法は、図8に示すように、電池組立工程Q1と、電解液注入工程S1と、第1液量計測工程S2と、電解液強制浸透工程S3と、初期充電工程Q2と、コンディショニング工程S6と、エージング工程S7と、第2液量計測工程S4と、評価工程S5と、外観検査工程Q3と、を順に施工する。 The manufacturing method for this nonaqueous electrolyte secondary battery 10 uses the above-described method SS for evaluating the inter-electrode distance DL of the nonaqueous electrolyte secondary battery 10. That is, as shown in FIG. 8, the manufacturing method for this nonaqueous electrolyte secondary battery 10 sequentially includes a battery assembly process Q1, an electrolyte injection process S1, a first liquid level measurement process S2, a forced electrolyte penetration process S3, an initial charging process Q2, a conditioning process S6, an aging process S7, a second liquid level measurement process S4, an evaluation process S5, and an appearance inspection process Q3.

ここで、電池組立工程Q1は、正極体11と負極体12とがセパレータ13を挟んで積層された電極体1をケース本体31内に収納し、ケース蓋体32を封口する工程である。この段階では、電解液2の注入口321は、開放されている。また、初期充電工程Q2は、電極体1を外部電源に接続して初回の充電を行い、電解液等の一部や電池内部に含まれる水分が分解することによって発生するガスをケース外に逃がす工程である。また、外観検査工程Q3は、外観上の傷等を検査して、出荷の可否を決める工程である。 The battery assembly process Q1 involves housing the electrode body 1, which is made up of a stack of cathode bodies 11 and anode bodies 12 sandwiched between separators 13, in the case body 31 and sealing the case lid 32. At this stage, the electrolyte 2 inlet 321 is open. The initial charging process Q2 involves connecting the electrode body 1 to an external power source for initial charging, allowing gas generated by decomposition of part of the electrolyte and water contained within the battery to escape outside the case. The appearance inspection process Q3 involves inspecting for external damage and determining whether or not the battery can be shipped.

そして、評価工程S5にて、電極体1の極間距離DLが適正と評価された非水電解液二次電池10が外観検査工程Q3に送られ、外観検査合格(OK)の場合に出荷される。これに対して、評価工程S5にて、電極体1の極間距離DLが不適正と評価された非水電解液二次電池10は、出荷停止となる。また、評価工程S5にて、電極体1の極間距離DLが適正と評価された非水電解液二次電池10でも、外観検査工程Q3にて外観検査不合格(NG)の場合には、出荷停止される。 Then, nonaqueous electrolyte secondary batteries 10 for which the inter-electrode distance DL of the electrode body 1 is evaluated as appropriate in the evaluation process S5 are sent to the visual inspection process Q3, and are shipped if they pass the visual inspection (OK). In contrast, nonaqueous electrolyte secondary batteries 10 for which the inter-electrode distance DL of the electrode body 1 is evaluated as inappropriate in the evaluation process S5 are suspended from shipment. Furthermore, even if the inter-electrode distance DL of the electrode body 1 is evaluated as appropriate in the evaluation process S5, if it fails the visual inspection (NG) in the visual inspection process Q3, they are also suspended from shipment.

以上のように、本非水電解液二次電池10の製造方法は、非水電解液二次電池10の製造工程において、非水電解液二次電池10の極間距離DLの評価方法SSを用いたので、すべての非水電解液二次電池10に対してデンドライト析出に関与する電極体1の極間距離DLの適否を評価できる。したがって、デンドライト析出耐性の優れた高品質な非水電解液二次電池を安定して提供することができる。 As described above, the manufacturing method for the nonaqueous electrolyte secondary battery 10 uses the evaluation method SS for the inter-electrode distance DL of the nonaqueous electrolyte secondary battery 10 during the manufacturing process of the nonaqueous electrolyte secondary battery 10, so the suitability of the inter-electrode distance DL of the electrode body 1, which is involved in dendrite precipitation, can be evaluated for all nonaqueous electrolyte secondary batteries 10. Therefore, it is possible to consistently provide high-quality nonaqueous electrolyte secondary batteries with excellent dendrite precipitation resistance.

<変形例>
以上、詳細に説明した本実施形態は、単なる例示にすぎず、本開示技術を何ら限定するものではない。したがって、本開示技術は、その要旨を逸脱しない範囲内で種々の改良、変形が可能である。
<Modification>
The present embodiment described in detail above is merely an example and does not limit the disclosed technology in any way. Therefore, the disclosed technology can be improved and modified in various ways without departing from the spirit and scope of the present invention.

1 電極体
2 非水電解液
2Y 余剰電解液
3 ケース
10、10B 非水電解液二次電池
11 正極体
12 負極体
13 セパレータ
DK 極間
DL 極間距離
KJ 基準値
L0、L1 液量
ΔL 液変化量
S1 電解液注入工程
S2 第1液量計測工程
S3 電解液強制浸透工程
S4 第2液量計測工程
S5 評価工程
S6 コンディショニング工程
S7 エージング工程
REFERENCE SIGNS LIST 1 Electrode body 2 Nonaqueous electrolyte 2Y Surplus electrolyte 3 Case 10, 10B Nonaqueous electrolyte secondary battery 11 Cathode body 12 Negative electrode body 13 Separator DK Interelectrode distance DL Interelectrode distance KJ Reference value L0, L1 Liquid volume ΔL Liquid change amount S1 Electrolyte injection step S2 First liquid volume measurement step S3 Electrolyte forced penetration step S4 Second liquid volume measurement step S5 Evaluation step S6 Conditioning step S7 Aging step

Claims (3)

正極体と負極体とがセパレータを挟んで積層された電極体と、前記電極体の極間に浸透した非水電解液と、前記非水電解液であって前記電極体の前記極間に浸透していない余剰電解液と、をケース内に収容した非水電解液二次電池の製造段階において、
前記ケース内に前記余剰電解液が残るように前記非水電解液を注入する電解液注入工程と、
前記ケース内の前記余剰電解液を前記電極体の前記極間に強制的に浸透させる電解液強制浸透工程と、
前記電解液注入工程後で、前記電解液強制浸透工程前に、前記ケース内の前記余剰電解液の液量を計測する第1液量計測工程と、
前記電解液強制浸透工程後に、前記ケース内の前記余剰電解液の液量を計測する第2液量計測工程と、
前記第1液量計測工程で計測した前記液量から前記第2液量計測工程で計測した前記液量を差し引いた前記余剰電解液の液変化量が、所定の基準値以下の場合に、前記電極体の極間距離が適正と評価する評価工程と、を備え
前記所定の基準値は、デンドライト析出耐性が良好となる前記液変化量の値である
非水電解液二次電池の極間距離の評価方法。
In a manufacturing stage of a nonaqueous electrolyte secondary battery, an electrode assembly in which a positive electrode body and a negative electrode body are stacked with a separator sandwiched therebetween, a nonaqueous electrolyte solution that has permeated between the electrodes of the electrode assembly, and excess electrolyte solution of the nonaqueous electrolyte solution that has not permeated between the electrodes of the electrode assembly are housed in a case,
an electrolyte injection step of injecting the nonaqueous electrolyte so that excess electrolyte remains in the case;
an electrolyte forced penetration step of forcibly penetrating the excess electrolyte in the case between the electrodes of the electrode body;
a first liquid volume measuring step of measuring the volume of the excess electrolyte in the case after the electrolyte injection step and before the electrolyte forced penetration step;
a second liquid volume measuring step of measuring the liquid volume of the excess electrolyte in the case after the electrolyte forced penetration step;
an evaluation step of evaluating the inter-electrode distance of the electrode body as appropriate when a change in the amount of excess electrolyte obtained by subtracting the amount of liquid measured in the second liquid volume measurement step from the amount of liquid measured in the first liquid volume measurement step is equal to or less than a predetermined reference value ,
The predetermined reference value is the value of the liquid change amount at which resistance to dendrite precipitation is good.
A method for evaluating the electrode distance of a non-aqueous electrolyte secondary battery.
請求項1に記載された非水電解液二次電池の極間距離の評価方法において、
前記第2液量計測工程は、前記電解液強制浸透工程後であって、前記非水電解液二次電池に対する常温下で複数回充放電を行うコンディショニング工程及び金属異物の溶解や前記コンディショニング工程にて前記負極体の表面近傍に前記電解液に由来して形成される保護被膜の安定化を行うことができるエージング工程の後に行う
非水電解液二次電池の極間距離の評価方法。
2. The method for evaluating the inter-electrode distance of a non-aqueous electrolyte secondary battery according to claim 1,
The second liquid volume measuring step is a method for evaluating an inter-electrode distance of a nonaqueous electrolyte secondary battery, which is performed after the electrolyte forced penetration step, a conditioning step in which the nonaqueous electrolyte secondary battery is charged and discharged multiple times at room temperature, and an aging step in which metallic foreign matter can be dissolved and a protective coating formed in the vicinity of the surface of the negative electrode body due to the electrolyte in the conditioning step can be stabilized .
請求項1又は請求項2に記載された非水電解液二次電池の極間距離の評価方法を用いた
非水電解液二次電池の製造方法。
3. A method for manufacturing a non-aqueous electrolyte secondary battery using the method for evaluating the inter-electrode distance of a non-aqueous electrolyte secondary battery according to claim 1.
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