JP2019021445A - Suppressing method of separator wrinkle in first charging method of lithium ion secondary battery and manufacturing method of lithium ion secondary battery - Google Patents
Suppressing method of separator wrinkle in first charging method of lithium ion secondary battery and manufacturing method of lithium ion secondary battery Download PDFInfo
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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Abstract
Description
本発明は、リチウムイオン二次電池の初回充電方法におけるセパレータ皺抑制方法および当該初回充電方法を含むリチウムイオン二次電池の製造方法に関する。 The present invention relates to a method for suppressing separator flaws in an initial charging method for a lithium ion secondary battery and a method for manufacturing a lithium ion secondary battery including the initial charging method.
二次電池は、携帯機器、電気自動車、住宅若しくは事業施設の電源として幅広い用途に展開されている。二次電池の中でリチウムイオン二次電池は、これらの用途に適した高い放電電圧を有するため、現在の二次電池の主流になっている。 Secondary batteries are used in a wide range of applications as power sources for portable devices, electric vehicles, houses, or business facilities. Among secondary batteries, a lithium ion secondary battery has a high discharge voltage suitable for these applications, and has become the mainstream of current secondary batteries.
リチウムイオン二次電池の製造工程の1つとして、初回充電がある。初回充電では、二次電池を構成する部材に含まれる微量な水分が電気分解する、および非水電解液を構成する有機溶媒の一部が分解する、ことによって、二次電池内にガスが発生する。発生したガスは、負極表面を安定化するSEI(Solid Electrolyte Interface)を形成するときの副生成物である。発生したガスが二次電池内に滞留したまま充放電を繰り返すと、二次電池の性能、安全性および信頼性を低下させる。 One of the manufacturing processes of a lithium ion secondary battery is initial charging. In the first charge, gas is generated in the secondary battery by electrolyzing a small amount of water contained in the members constituting the secondary battery and by partially decomposing the organic solvent constituting the non-aqueous electrolyte. To do. The generated gas is a by-product when forming SEI (Solid Electrolyte Interface) that stabilizes the negative electrode surface. If charging and discharging are repeated while the generated gas stays in the secondary battery, the performance, safety and reliability of the secondary battery are lowered.
特許文献1〜4には、発生したガスに伴う二次電池の性能、安全性および信頼性の低下を解決するための方法等が記載されている。
しかしながら、前記特許文献1〜4に記載の方法では電極板間に滞留しているガスを適切に除去することが困難である。また、特許文献1〜4に記載の方法は最近における様々な電池材料が開発されたことに伴い、従来の電池電圧とは異なる電池系や使用する電解液の組成及び添加剤の種類によりガス発生のタイミングが変わるため、適用できないこと場合もある。
However, in the methods described in
さらに、前記特許文献1〜4に記載の方法はガス発生に伴い、正極と負極の間に介在する絶縁性のセパレータの皺発生を効果的に抑制できない。
Furthermore, the methods described in
すなわち、初回充電時に充電が不均一になった二次電池は正極と負極の間に介在するセパレータに皺が発生する現象が多く見られる。充電が不均一な部分は、充電が進むに従って充電が均一な部分と比較してクレーターのような窪みが生じて土手のような形状になる。当該窪みは、ガスが滞留し易いため、滞留しているガスの内圧のストレスによりセパレータに皺が発生する。充電が不均一な部分に沿ってセパレータに皺が発生すると、充放電時における電池反応が著しく阻害される可能性がある。例えば、充放電の繰り返しによりセパレータの皺に沿ってリチウムの析出が起こり、二次電池の安全性および信頼性が低下する課題がある。 That is, a secondary battery in which charging is not uniform at the time of initial charging often has a phenomenon in which wrinkles are generated in the separator interposed between the positive electrode and the negative electrode. A portion where charging is not uniform becomes a bank like a crater-like depression as compared with a portion where charging is uniform as charging progresses. Since the gas tends to stay in the depression, wrinkles are generated in the separator due to the internal pressure stress of the staying gas. If wrinkles occur in the separator along the non-uniformly charged portion, the battery reaction during charging / discharging may be significantly inhibited. For example, there is a problem that lithium is deposited along the edge of the separator due to repeated charge and discharge, and the safety and reliability of the secondary battery are lowered.
本発明は、初回充電時の充電を均一化してセパレータの皺発生を効果的に抑制するリチウムイオン二次電池の初回充電方法におけるセパレータ皺抑制方法、および当該初回充電方法を含むリチウムイオン二次電池の製造方法を提供することを目的とする。 The present invention relates to a method for suppressing separator wrinkles in an initial charging method of a lithium ion secondary battery that effectively suppresses generation of wrinkles of the separator by uniformizing charging at the time of initial charging, and a lithium ion secondary battery including the initial charging method It aims at providing the manufacturing method of.
上記の課題を解決するために、本発明の実施形態によると、外装体と、当該外装体内に収納され、セパレータを挟んで正極および負極を交互に積層した電極群と、前記外装体内に収容された非水電解液とを備えたリチウムイオン二次電池の初回充電方法におけるセパレータ皺抑制方法であって、
前記初回充電は、前記電極群を収納した前記外装体内に前記非水電解液を注入した後、当該外装体を封止して密閉した状態で少なくとも2回の充電工程を含み、
1回目の充電工程後に静置し、2回目の充電工程後にガス排気を行うことを特徴とするリチウムイオン二次電池の初回充電方法におけるセパレータ皺抑制方法が提供される。
In order to solve the above-described problem, according to an embodiment of the present invention, an exterior body, an electrode group that is housed in the exterior body, in which a positive electrode and a negative electrode are alternately stacked with a separator interposed therebetween, and the exterior body are housed. A separator soot suppression method in the initial charging method of a lithium ion secondary battery provided with a non-aqueous electrolyte,
The initial charging includes at least two charging steps in a state where the outer body is sealed and sealed after injecting the non-aqueous electrolyte into the outer body housing the electrode group,
There is provided a method for suppressing separator flaws in an initial charging method of a lithium ion secondary battery, characterized in that the apparatus is left after the first charging step and gas is exhausted after the second charging step.
本発明によれば、セパレータの皺発生を効果的に抑制することによって、充放電の繰り返しに伴うリチウムの析出を抑制して寿命末期状態でのリチウムイオン二次電池の安全性と信頼性を確保することが可能なリチウムイオン二次電池の初回充電方法におけるセパレータ皺抑制方法、および当該初回充電方法を含み、簡単な工程で安全性と信頼性を確保することが可能なリチウムイオン二次電池の製造方法を提供できる。 According to the present invention, by effectively suppressing the occurrence of wrinkles in the separator, lithium deposition associated with repeated charging and discharging is suppressed, and the safety and reliability of the lithium ion secondary battery in the end of life state are ensured. Of a lithium ion secondary battery capable of ensuring safety and reliability in a simple process, including a separator flaw suppression method in the initial charging method of a lithium ion secondary battery that can be performed, and the initial charging method A manufacturing method can be provided.
以下、実施形態に係るリチウムイオン二次電池の初回充電方法におけるセパレータ皺抑制方法を詳細に説明する。 Hereinafter, the separator flaw suppression method in the initial charge method of the lithium ion secondary battery according to the embodiment will be described in detail.
最初に、外装体と電極群を用意し、当該電極群を外装体内に収納する。電極群は、セパレータを挟んで正極および負極を交互に複数積層した構造を有する。電極群を収納した外装体内に非水電解液を注入し、当該外装体を封止して密閉状態にした後、リチウムイオン二次電池の初回の充電を開始する。なお、二次電池の組み立て直後、初回充電前に二次電池を例えば0.1〜100kgf/cm2の圧力で加圧することが好ましい。このような前処理を施すことによって、セパレータの皺発生をより効果的に防ぐことが可能になる。また、加圧処理後、初回充電前に静置することによって、非水電解液を電極群の構成部材になじませることが可能になる。 First, an exterior body and an electrode group are prepared, and the electrode group is accommodated in the exterior body. The electrode group has a structure in which a plurality of positive electrodes and negative electrodes are alternately stacked with a separator interposed therebetween. A non-aqueous electrolyte is injected into the exterior body containing the electrode group, and the exterior body is sealed and sealed, and then the first charge of the lithium ion secondary battery is started. In addition, it is preferable to pressurize a secondary battery with the pressure of 0.1-100 kgf / cm < 2 > immediately after the assembly of a secondary battery and before first charge. By performing such pretreatment, it is possible to more effectively prevent the occurrence of wrinkles in the separator. Moreover, it becomes possible to let a nonaqueous electrolyte solution adapt to the structural member of an electrode group by leaving still after a pressurization process and before first charge.
初回の充電は、二次電池と充電装置とを接続することにより行う。1回目の充電を終了した後、二次電池と充電装置とを遮断し、静置させる。その後、2回目の充電に移行させ、当該二次電池が満充電状態に至る前に、外装体内に発生したガスを排気する。 The first charging is performed by connecting the secondary battery and the charging device. After completing the first charge, the secondary battery and the charging device are shut off and allowed to stand. Thereafter, the second charging is performed, and the gas generated in the exterior body is exhausted before the secondary battery reaches a fully charged state.
ここで、満充電とは当該二次電池の定格容量に相当する充電電気量が100%充電された充電状態(State Of Charge: SOC)を言う。 Here, the full charge refers to a state of charge (SOC) in which the amount of charge corresponding to the rated capacity of the secondary battery is 100% charged.
1回目の充電が適用される二次電池は、外装体内の電極群の正極および負極が一度も使用されず、最適化されていない、つまり非水電解液が電極群に十分に含侵されていない状態である。このような二次電池に1回目の充電を行うと、過電圧による負極表面へのリチウムの電析が起こる可能性があること、および負極表面にSEI膜を生成すること、から慎重に実行する必要がある。SEI膜は、負極表面の炭素材と非水電解液との過度の反応を抑制し、負極表面での反応を安定させる。SEI膜の生成は、公知の事実であるものの、初回充電時、1.2〜0.8V(vs.Li/Li+)の負極電位である。しかしながら、初回充電時では当該電位の保持時間が短く、負極表面にSEI膜を十分に形成することが困難になる。 In the secondary battery to which the first charging is applied, the positive electrode and the negative electrode of the electrode group in the outer package are never used and are not optimized, that is, the non-aqueous electrolyte is sufficiently impregnated in the electrode group. There is no state. When such a secondary battery is charged for the first time, lithium may be electrodeposited on the negative electrode surface due to overvoltage, and an SEI film must be formed on the negative electrode surface. There is. The SEI film suppresses excessive reaction between the carbon material on the negative electrode surface and the non-aqueous electrolyte, and stabilizes the reaction on the negative electrode surface. Although the generation of the SEI film is a known fact, it has a negative electrode potential of 1.2 to 0.8 V (vs. Li / Li + ) at the first charge. However, at the time of the initial charge, the potential holding time is short, and it becomes difficult to sufficiently form the SEI film on the negative electrode surface.
このようなことから、1回目の充電工程は当該1回目の充電開始後の充電曲線、ここで横軸は電池電圧V、縦軸は蓄電量変化量[Ah]/電池電圧変化量[V](dQ/dV)である、1回目の充電工程において少なくとも1つの変曲点が現れる条件で実行することが好ましい。図1に、初回充電における1回目の充電開始後の充電曲線を示す。図1に示す変曲点は、ある容量範囲の間でのピークであり、SEI膜の生成反応のピークであると推定される。ピークが収まる充電電気量は、充電時の電流値にも依存するが、二次電池の定格容量の約1〜5%の範囲内に出現する。このため、1回目の充電工程の充電電気量は二次電池の定格容量の1〜5%の範囲で行うことが好ましい。1回目の充電工程を充電開始後の充電曲線において、変曲点が現れる条件、つまり充電電気量が二次電池の定格容量の1〜5%の範囲、でかつ低電流値(≦0.1ItA)にて行うことによって、負極表面に緻密なSEI膜を形成することが可能になる。 For this reason, the first charging step is the charging curve after the start of the first charging, where the horizontal axis is the battery voltage V, and the vertical axis is the amount of change in charge [Ah] / the amount of change in battery voltage [V]. It is preferable that the process is performed under the condition that at least one inflection point appears in the first charging step, which is (dQ / dV). FIG. 1 shows a charge curve after the first charge start in the first charge. The inflection point shown in FIG. 1 is a peak between a certain capacity range, and is presumed to be a peak of the formation reaction of the SEI film. The amount of charged electricity at which the peak falls depends on the current value at the time of charging, but appears within a range of about 1 to 5% of the rated capacity of the secondary battery. For this reason, it is preferable to perform the amount of charge electricity of the 1st charge process in the range of 1-5% of the rated capacity of a secondary battery. In the charging curve after the start of charging in the first charging step, a condition where an inflection point appears, that is, the amount of charged electricity is in the range of 1 to 5% of the rated capacity of the secondary battery, and a low current value (≦ 0.1 ItA ), A dense SEI film can be formed on the negative electrode surface.
1回目の充電工程後に静置させることによって、電極(正極および負極)の細孔部への非水電解液の含浸をより一層促進することができる。その結果、電極表面での非水電解液の還元を抑制し、不均一な電極反応も抑制することができる。静置の時間は、8〜24時間程度にすることが好ましい。 By allowing it to stand after the first charging step, the impregnation of the nonaqueous electrolyte into the pores of the electrodes (positive electrode and negative electrode) can be further promoted. As a result, the reduction of the nonaqueous electrolytic solution on the electrode surface can be suppressed, and a nonuniform electrode reaction can also be suppressed. The standing time is preferably about 8 to 24 hours.
2回目の充電工程は、1回目の充電工程と静置工程を経た後に行うため、1回目の充電工程に比べて大きな電流値で実行できる。2回目の充電工程の役割は、外装体内に十分にガスを発生させることにある。このため、2回目の充電工程の充電電気量は、1回目の充電工程に比べて高くすることが好ましい。具体的には、2回目の充電工程の充電電気量はガスの発生程度にもよるが、二次電池の定格容量の38〜78%にすることが望ましい。 Since the second charging step is performed after passing through the first charging step and the stationary step, the second charging step can be executed with a larger current value than the first charging step. The role of the second charging step is to sufficiently generate gas in the exterior body. For this reason, it is preferable that the amount of charged electricity in the second charging step is higher than that in the first charging step. Specifically, the amount of electricity charged in the second charging process is preferably 38 to 78% of the rated capacity of the secondary battery, although it depends on the degree of gas generation.
2回目の充電工程による外装体内でのガス発生が終息した後、ガスの排気工程に移行する。排気工程は、公知方法によって二次電池の封止を一時的に解除して、外装体内のガスを排気する。ガスの排気工程は乾燥環境で行うことが好ましい。また、排気工程は外装体に外部から圧力を加えたり、二次電池をチャンバ内に入れて減圧したり、してガスの排気を促進させることによって、排気時間を短縮することができる。 After the gas generation in the exterior body by the second charging process ends, the process proceeds to the gas exhausting process. In the exhaust process, the sealing of the secondary battery is temporarily released by a known method, and the gas in the exterior body is exhausted. The gas exhaust step is preferably performed in a dry environment. Further, in the exhaust process, the exhaust time can be shortened by applying pressure to the exterior body from the outside, or by reducing the pressure by putting the secondary battery in the chamber, thereby facilitating exhaust of the gas.
3回目の充電工程は、2回目の充電工程の電流値と同じ条件下で、製造者が決定した上限電圧まで充電する、つまり前記1回目および2回目の充電工程を含めた満充電を行う。ただし、3回目以降の充電工程は必ずしも必要とせず、省略してもよい。 In the third charging step, charging is performed up to the upper limit voltage determined by the manufacturer under the same conditions as the current value in the second charging step, that is, full charging including the first charging step and the second charging step is performed. However, the third and subsequent charging steps are not necessarily required and may be omitted.
次に、前述したリチウムイオン二次電池の各部材を詳細に説明する。 Next, each member of the lithium ion secondary battery described above will be described in detail.
<外装体>
外装体は、熱融着性樹脂フィルム(内層)、金属箔、少なくとも1層の保護樹脂フィルム(外層)の順に積層した積層フィルムを用いた、袋形状をなす。内層は、ポリオレフィン系樹脂から形成され得る。金属層は、アルミニウム箔、ステンレス箔から形成され得る。外層は、ナイロン単体、ポリエチレンテレフタレート(PET)単体、またはナイロンとPETの積層膜から形成され得る。
<Exterior body>
The exterior body has a bag shape using a laminated film in which a heat-fusible resin film (inner layer), a metal foil, and at least one protective resin film (outer layer) are laminated in this order. The inner layer can be formed from a polyolefin-based resin. The metal layer can be formed from aluminum foil or stainless steel foil. The outer layer can be formed from nylon alone, polyethylene terephthalate (PET) alone, or a laminated film of nylon and PET.
<正極>
正極は、集電体と、集電体の少なくとも一方の面に形成され、正極活物質、導電材、結着材を含む正極層とを備える。
<Positive electrode>
The positive electrode includes a current collector and a positive electrode layer formed on at least one surface of the current collector and including a positive electrode active material, a conductive material, and a binder.
集電体は、例えばアルミニウム箔、銅箔またはステンレス箔などの金属箔、多孔質アルミニウムなどの多孔質金属などを用いることができる。 As the current collector, for example, a metal foil such as an aluminum foil, a copper foil or a stainless steel foil, a porous metal such as porous aluminum, or the like can be used.
正極活物質は、リチウムイオン二次電池に使用できるものであれば特に制限されず、例えばLiCoO2、LiNiO2、LiMn2O4、LiFePO4、LiCo1/3Ni1/3Mn1/3O2、LiCo0.15Ni0.8Al0.05O2、LiNi0.5Mn1.5O4を用いることができる。 The positive electrode active material is not particularly limited as long as it can be used for a lithium ion secondary battery. For example, LiCoO 2 , LiNiO 2 , LiMn 2 O 4 , LiFePO 4 , LiCo 1/3 Ni 1/3 Mn 1/3 O 2 , LiCo 0.15 Ni 0.8 Al 0.05 O 2 , LiNi 0.5 Mn 1.5 O 4 can be used.
導電材は、特に限定されるものではなく、公知または市販のものを使用することができる。例えば、アセチレンブラック、ケッチェンブラックなどのカーボンブラック、カーボンナノチューブ、炭素繊維、活性炭、黒鉛等が挙げられる。 The conductive material is not particularly limited, and a known or commercially available material can be used. Examples thereof include carbon black such as acetylene black and ketjen black, carbon nanotube, carbon fiber, activated carbon, graphite and the like.
結着材は、特に限定されるものではなく、公知または市販のものを使用することができる。例えば、ポリフッ化ビニリデン、ポリテトラフルオロエチレン(PTFE)、ポリビニルピロリドン(PVP)、ポリ塩化ビニル(PVC)、ポリエチレン(PE)、ポリプロピレン(PP)、エチレン−プロピレン共重合体、スチレンブタジエンゴム(SBR)、アクリル樹脂等が挙げられる。 A binder is not specifically limited, A well-known or commercially available thing can be used. For example, polyvinylidene fluoride, polytetrafluoroethylene (PTFE), polyvinylpyrrolidone (PVP), polyvinyl chloride (PVC), polyethylene (PE), polypropylene (PP), ethylene-propylene copolymer, styrene butadiene rubber (SBR) And acrylic resin.
正極層は、増粘剤または分散剤を更に含むことを許容する。増粘剤の例は、セルロース硫酸ナトリウム、メチルセルロースエーテル、メチルエチルセルロースエーテル、エチルセルロースエーテル、カルボキシメチルセルロースエーテルを含む。分散剤の例は、カチオン系界面活性剤、ノニオン系界面活性剤を含む。 The positive electrode layer is allowed to further contain a thickener or dispersant. Examples of thickeners include sodium cellulose sulfate, methyl cellulose ether, methyl ethyl cellulose ether, ethyl cellulose ether, carboxymethyl cellulose ether. Examples of the dispersant include a cationic surfactant and a nonionic surfactant.
正極は、例えば集電体の少なくとも一方の面に正極活物質、導電材、結着材および溶剤を含むスラリーを塗布して塗布膜を形成した後、乾燥、加圧することにより作製することができる。 The positive electrode can be produced, for example, by applying a slurry containing a positive electrode active material, a conductive material, a binder and a solvent to at least one surface of a current collector to form a coating film, and then drying and pressurizing. .
溶剤は、特に限定されるものではなく、公知または市販のものを使用できる。溶剤は、結着材としてポリフッ化ビニリデンを用いる場合、N−メチル−2−ピロリドンを用いることが好ましい。溶剤は、結着材としてスチレンブタジエンゴム(SBR)、ポリテトラフルオロエチレン、ポリビニルアルコール、カルボキシメチルセルロース等を用いる場合、水を用いることが好ましい。 The solvent is not particularly limited, and known or commercially available solvents can be used. The solvent is preferably N-methyl-2-pyrrolidone when polyvinylidene fluoride is used as the binder. The solvent is preferably water when styrene butadiene rubber (SBR), polytetrafluoroethylene, polyvinyl alcohol, carboxymethyl cellulose or the like is used as the binder.
<負極>
負極は、集電体と、集電体の少なくとも一方の面に形成され、負極活物質、導電材、結着材を含む負極層とを備える。
<Negative electrode>
The negative electrode includes a current collector and a negative electrode layer formed on at least one surface of the current collector and including a negative electrode active material, a conductive material, and a binder.
集電体は、特に限定されるものではないが、アルミニウム箔、銅箔またはステンレス箔などの金属箔、多孔質アルミニウム等を用いることができる。 The current collector is not particularly limited, and a metal foil such as an aluminum foil, a copper foil or a stainless steel foil, porous aluminum or the like can be used.
負極活物質は、特に制限されるものではなく、例えば、天然黒鉛または人造黒鉛、メソカーボンマイクロビーズ(MCMB)、ハードカーボンまたはソフトカーボンなどの炭素材料、Al、Si、Snなどのリチウムを吸蔵放出することができる金属材料またはその合金材料、SiO、SiO2、チタン酸リチウム(Li4Ti5012)などの酸化物材料などを用いることができる。 The negative electrode active material is not particularly limited. For example, natural graphite or artificial graphite, mesocarbon microbeads (MCMB), carbon materials such as hard carbon or soft carbon, and lithium such as Al, Si, and Sn are occluded and released. Metal materials that can be used or alloy materials thereof, oxide materials such as SiO, SiO 2 , and lithium titanate (Li 4 Ti 5 0 12 ) can be used.
結着材は、特に制限されるものではなく、例えばポリテトラフルオロエチレン(PTFE)、ポリフッ化ビニリデン、フッ素系ゴム、スチレンブタジエンゴム(SBR)、カルボキシルメチルセルロース(CMC)、コアシェルバインダー、ポリビニルアルコール、ポリイミド、ポリアミドイミドなどを用いることができる。 The binder is not particularly limited. For example, polytetrafluoroethylene (PTFE), polyvinylidene fluoride, fluorine rubber, styrene butadiene rubber (SBR), carboxymethyl cellulose (CMC), core shell binder, polyvinyl alcohol, polyimide Polyamideimide or the like can be used.
導電材は、前述した正極に用いるものと同様のもの、例えばアセチレンブラック、ケッチェンブラック等のカーボンブラック、活性炭または黒鉛などを用いることができる。なお、導電剤は負極層に含まれなくてもよい。 As the conductive material, the same materials as those used for the positive electrode described above, for example, carbon black such as acetylene black and ketjen black, activated carbon or graphite can be used. Note that the conductive agent may not be included in the negative electrode layer.
<セパレータ>
セパレータは、ポリエチレン(PE)、ポリプロピレン(PP)のようなポリオレフィンまたはポリテトラフルオロエチレン(PTFE)等の合成樹脂からなる不織布または多孔性シートを使用できる。
<Separator>
As the separator, a nonwoven fabric or a porous sheet made of a synthetic resin such as polyolefin such as polyethylene (PE) or polypropylene (PP) or polytetrafluoroethylene (PTFE) can be used.
<非水電解液>
非水電解液は、リチウムイオンを含む電解質塩と有機溶媒とを含む。
<Non-aqueous electrolyte>
The nonaqueous electrolytic solution contains an electrolyte salt containing lithium ions and an organic solvent.
電解質塩は、特に限定されず、公知のリチウム塩が適用可能である。例えば、LiBF4、LiPF6、LiAsF6、LiCF3CFO、LiSO3CF3、LiCF2CF2SO3、LiClO4、LiN(COCF2CF3)2、LiN(SO2CF3)2等のリチウム塩を挙げることができる。これらリチウム塩は、1種または2種以上の混合物で使用することができる。 The electrolyte salt is not particularly limited, and a known lithium salt can be applied. For example, lithium such as LiBF 4 , LiPF 6 , LiAsF 6 , LiCF 3 CFO, LiSO 3 CF 3 , LiCF 2 CF 2 SO 3 , LiClO 4 , LiN (COCF 2 CF 3 ) 2 , LiN (SO 2 CF 3 ) 2 Mention may be made of salts. These lithium salts can be used alone or in a mixture of two or more.
溶媒は、主溶媒と副溶媒の混合溶媒であることが好ましい。主溶媒は、例えばエチレンカーボネート、γブチロラクトン、ジエチルカーボネート、ジメチルカーボネートを用いることができる。副溶媒は、プロピレンカーボネイト、スルホラン、ジメトキシエタン、ジエトキシエタン、2−メチル−テトラヒドロフラン、各種グライム類等を用いることができる。 The solvent is preferably a mixed solvent of a main solvent and a sub solvent. As the main solvent, for example, ethylene carbonate, γ-butyrolactone, diethyl carbonate, or dimethyl carbonate can be used. As the auxiliary solvent, propylene carbonate, sulfolane, dimethoxyethane, diethoxyethane, 2-methyl-tetrahydrofuran, various glymes and the like can be used.
溶媒中に溶解される電解質塩の濃度は、特に限定されず、例えば0.3モル/L〜3.0モル/Lであることが好ましい。 The concentration of the electrolyte salt dissolved in the solvent is not particularly limited, and is preferably, for example, 0.3 mol / L to 3.0 mol / L.
非水電解液は、分子内に不飽和結合を有し、充電時に還元重合が可能な有機物をさらに含むことを許容する。このような有機物を非水電解液に添加することによって、負極活物質の表面に有効な固体電解質界面被膜を形成することができ、非水電解液の分解を抑制することが可能となる。分子内に不飽和結合を有し、充電時に還元重合が可能な有機物は、例えばフルオロエチレンカーボネート、ビニレンカーボネート(VC)、ビニルエチレンカーボネートのようなカーボネート及びその誘導体、不飽和のカルボン酸エステル類、リン酸エステル類、ホウ酸エステル類、またはアルコール類等を用いることができる。中でも、ビニレンカーボネート(VC)を用いるのが好ましい。このような有機物は、安定な固体電解質界面被膜を得るために、非水電解質に対して0.1重量%〜10重量%、より好ましくは1重量%〜5重量%添加することが望ましい。前記有機物の添加量を0.1重量%〜10重量%の範囲にすることによって、充電時に還元されて、負極活物質層の表面に安定な被膜を形成することができ、電解質材料の分解を防ぐことができる。有機物の添加量が0.1重量%未満の場合は、負極活物質の表面に安定な被膜を十分に形成するのが困難となる。他方、有機物の添加量が10重量%を超える場合には、還元される量が増えるため、形成される固体電解質界面被膜が厚くなり、電池のインピーダンスが上昇する虞がある。 The nonaqueous electrolyte solution further includes an organic substance having an unsaturated bond in the molecule and capable of reductive polymerization at the time of charging. By adding such an organic substance to the non-aqueous electrolyte, an effective solid electrolyte interface coating can be formed on the surface of the negative electrode active material, and decomposition of the non-aqueous electrolyte can be suppressed. Organic substances having an unsaturated bond in the molecule and capable of reductive polymerization at the time of charging are, for example, fluoroethylene carbonate, vinylene carbonate (VC), carbonates such as vinyl ethylene carbonate and derivatives thereof, unsaturated carboxylic acid esters, Phosphate esters, borate esters, alcohols, and the like can be used. Among these, it is preferable to use vinylene carbonate (VC). In order to obtain a stable solid electrolyte interface coating, such an organic substance is desirably added in an amount of 0.1 wt% to 10 wt%, more preferably 1 wt% to 5 wt% with respect to the nonaqueous electrolyte. By making the addition amount of the organic substance in the range of 0.1 wt% to 10 wt%, it can be reduced at the time of charging to form a stable film on the surface of the negative electrode active material layer, and the electrolyte material can be decomposed. Can be prevented. When the amount of the organic substance added is less than 0.1% by weight, it is difficult to sufficiently form a stable film on the surface of the negative electrode active material. On the other hand, when the amount of the organic substance added exceeds 10% by weight, the amount to be reduced increases, so that the formed solid electrolyte interface film becomes thick and the battery impedance may increase.
実施形態に係るリチウムイオン二次電池の製造方法は、前述したリチウムイオン二次電池の初回充電方法を含む。 The manufacturing method of the lithium ion secondary battery which concerns on embodiment contains the initial charging method of the lithium ion secondary battery mentioned above.
実施形態に係る方法により製造されるリチウム二次電池の形状は特に限定されないが、例えばコイン型、ボタン型、シート型、積層型、円筒型、角形、扁平型等が挙げられる。 The shape of the lithium secondary battery manufactured by the method according to the embodiment is not particularly limited, and examples thereof include a coin type, a button type, a sheet type, a stacked type, a cylindrical type, a rectangular shape, and a flat type.
以下、積層型のリチウム二次電池を例にして、実施形態に係るリチウム二次電池の構造を、図面を参照して説明する。図2は、積層型のリチウム二次電池の一例を示す斜視図、図3は図2のIII−III線に沿う断面図である。 Hereinafter, the structure of the lithium secondary battery according to the embodiment will be described with reference to the drawings, taking a laminated lithium secondary battery as an example. FIG. 2 is a perspective view showing an example of a stacked lithium secondary battery, and FIG. 3 is a cross-sectional view taken along line III-III in FIG.
積層型のリチウム二次電池1は、ラミネートフィルムからなる袋状の外装体2を備えている。外装体2内には、扁平状の電極群3が収納されている。ラミネートフィルムは、例えば複数枚(例えば2枚)のプラスチックフィルムをそれらのフィルム間にアルミニウム箔のような金属箔を挟んで積層した構造を有する。2枚のプラスチックフィルムのうち、一方のプラスチックフィルムは熱融着性樹脂フィルムが用いられる。外装体2は、2枚のラミネートフィルムを熱融着性樹脂フィルムが互いに対向するように重ね、これらのラミネートフィルム間に電極群3を介在し、電極群3周辺の2枚のラミネートフィルム部分を互いに熱融着して封止することにより、前記電極群3を気密に収納している。
The laminated lithium
電極群3は、図3に示すように正極4と負極5とそれら正極4、負極5の間に介在されたセパレータ6を負極5が最外層に位置するように複数積層した構造を有する。正極4は、正極集電体41と当該集電体41の両面に形成された正極層42,42とから構成されている。最外層に位置する負極5は、負極集電体51と、当該集電体51のセパレータ6と対向する面に形成された負極層52とから構成されている。最外層に位置する負極5を除く、正極4間に位置する負極5は、負極集電体51と、当該集電体51の両面に形成された金属リチウムからなる負極層52,52とから構成されている。
As shown in FIG. 3, the
正極4は、正極集電体41が正極層42の例えば右側面から延出した正極リード43を有する。各正極リード43は、外装体2内において先端側で束ねられ、互いに接合されている。正極端子7は、一端が正極リード43の接合部に接合され、かつ他端が外装体2の封止部を通して外部に延出している。負極5は、負極集電体51が負極層52の例えば左側面から延出した負極リード53を有する。各負極リード53は、外装体2内において先端側で束ねられ、互いに接合されている。負極端子8は、一端が負極リード53の接合部に接合され、かつ他端が外装体2の封止部を通して外部に延出している。
The positive electrode 4 includes a
以下、実施例を詳細に説明する。 Examples will be described in detail below.
(実施例1)
<正極>
リン酸鉄リチウム(LiFePO4)90質量部と、ポリフッ化ビニリデン5質量部と、導電材であるカーボンブラック5質量部とをN−メチルピロリドン(NMP)に溶解、分散させて正極スラリーを調製した。この正極スラリーを厚さ20μmのアルミニウム箔の両面に塗布し、乾燥した後、加圧することによって正極を得た。
Example 1
<Positive electrode>
90 parts by mass of lithium iron phosphate (LiFePO 4 ), 5 parts by mass of polyvinylidene fluoride, and 5 parts by mass of carbon black as a conductive material were dissolved and dispersed in N-methylpyrrolidone (NMP) to prepare a positive electrode slurry. . This positive electrode slurry was applied to both sides of an aluminum foil having a thickness of 20 μm, dried, and then pressurized to obtain a positive electrode.
<負極>
黒鉛98質量部と、カルボキシルメチルセルロース(CMC)1質量部と、スチレンブタジエンラバー(SBR)1重量部と溶剤であるイオン交換水に分散させて負極スラリーを調製した。この負極スラリーを厚さ10μmの銅箔の両面に塗布し、乾燥した後、加圧することによって負極を得た。
<Negative electrode>
A negative electrode slurry was prepared by dispersing in 98 parts by weight of graphite, 1 part by weight of carboxymethyl cellulose (CMC), 1 part by weight of styrene butadiene rubber (SBR) and ion-exchanged water as a solvent. This negative electrode slurry was applied to both sides of a copper foil having a thickness of 10 μm, dried, and then pressurized to obtain a negative electrode.
<セパレータ>
乾式一軸延伸法で得たポリエチレンフィルムを2枚のポリプロピレンフィルムで挟み込んだ、厚さ25μmの3層フィルムに多数の微細孔を開孔してセパレータを作製した。タイプであり、を用いた。
<Separator>
A separator was prepared by opening a large number of fine holes in a three-layer film having a thickness of 25 μm in which a polyethylene film obtained by a dry uniaxial stretching method was sandwiched between two polypropylene films. The type is used.
<非水電解液>
非水電解液には、エチレンカーボネート(EC)、エチルメチルカーボネート(EMC)およびジメチルカーボネート(DMC)の混合溶媒(体積比で2:5:3)にLiPF6を1.3モル/L溶解させ、添加剤としてビニレンカーボネイト(VC)を3重量%添加して調製した。
<Non-aqueous electrolyte>
In the non-aqueous electrolyte, 1.3 mol / L of LiPF 6 was dissolved in a mixed solvent of ethylene carbonate (EC), ethyl methyl carbonate (EMC) and dimethyl carbonate (DMC) (volume ratio 2: 5: 3). In addition, 3% by weight of vinylene carbonate (VC) was added as an additive.
<Alラミネート>
厚さ80μmのポリオレフィン系樹脂からなる熱融着性を有する内層と、厚さ40μmのアルミニウム箔からなる中間層と、ポリエチレンテレフタレートからなる外層とをこの順序で積層してAlラミネートを作製した。このAlラミネートは、総厚さ153μmであった。
<Al laminate>
An Al laminate was produced by laminating an inner layer made of a polyolefin resin having a thickness of 80 μm, a heat-fusible inner layer, an intermediate layer made of an aluminum foil having a thickness of 40 μm, and an outer layer made of polyethylene terephthalate in this order. This Al laminate had a total thickness of 153 μm.
<リチウムイオン二次電池の組立>
所定の寸法にカットした正極とセパレータを正極1枚に対してセパレータ2枚で覆った。セパレータは、正極に熱溶着して剥がれないようにした。この正極とセパレータの組合せ7枚と負極8枚を交互に積層し、積層電極群を得た。この積層電極群は、電池容量で3Ah程度であった。
<Assembly of lithium ion secondary battery>
A positive electrode and a separator cut to a predetermined size were covered with two separators with respect to one positive electrode. The separator was thermally welded to the positive electrode so as not to peel off. Seven combinations of the positive electrode and the separator and eight negative electrodes were alternately stacked to obtain a stacked electrode group. This laminated electrode group had a battery capacity of about 3 Ah.
積層電極群の正極の正極層未形成部および負極の負極層未形成部にそれぞれ端子用タブを超音波溶接によって接続した。このタブ付積層電極群を2枚のAlラミネートフィルムで前記端子用タブが外部に突出するように、熱融着性を有する内層が互いに対向するように挟み、Alラミネートフィルムの周辺三辺に位置する熱融着性を有する内層を熱溶着して外装体とした。封止せずに残した外装体の一辺から非水電解液を注入した後、真空封止して密閉状態のリチウムイオン二次電池を得た。非水電解液量は、7〜8g/Ah程度で調整した。封止工程の減圧度(真空度)は、1hPaとした。 Terminal tabs were connected to the positive electrode unformed part of the positive electrode and the negative electrode non-formed part of the negative electrode of the laminated electrode group, respectively, by ultrasonic welding. The laminated electrode group with tabs is sandwiched between two Al laminate films so that the terminal tabs protrude to the outside so that the inner layers having heat-fusibility are opposed to each other, and positioned on the three sides of the Al laminate film. The inner layer having the heat-fusibility is thermally welded to obtain an outer package. After injecting a non-aqueous electrolyte from one side of the outer package that was left unsealed, it was vacuum sealed to obtain a sealed lithium ion secondary battery. The amount of the non-aqueous electrolyte was adjusted at about 7 to 8 g / Ah. The degree of vacuum (degree of vacuum) in the sealing process was 1 hPa.
封止工程直後のリチウムイオン二次電池を1kgf/cm2の圧力で加圧し、その後加圧状態を維持しながら、3時間静置させた。 The lithium ion secondary battery immediately after the sealing step was pressurized at a pressure of 1 kgf / cm 2 and then allowed to stand for 3 hours while maintaining the pressurized state.
次いで、密閉状態のリチウムイオン二次電池を初回充電した。初回充電の条件は、以下の通りである。 Next, the sealed lithium ion secondary battery was charged for the first time. The conditions for the first charge are as follows.
1)1回目の充電工程は加圧状態を維持しながら、0.01ItAで2時間を行った。 1) The first charging step was performed at 0.01 ItA for 2 hours while maintaining the pressurized state.
2)1回目の充電工程後、加圧状態を維持しながら、16時間の静置を行った。 2) After the 1st charge process, it left still for 16 hours, maintaining a pressurization state.
3)2回目の充電工程は加圧状態を維持しながら、0.057ItAで8.4時間行った。2回目の充電工程までの充電電気量は、定格容量の50%とした。 3) The second charging step was carried out at 0.057 ItA for 8.4 hours while maintaining the pressurized state. The amount of electricity charged until the second charging step was 50% of the rated capacity.
4)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 4) The gas exhaust process was performed by releasing the pressure applied to the secondary battery and further temporarily releasing the sealing.
5)3回目の充電工程は、リチウムイオン二次電池を再度、密閉状態にし、前記と同じ圧力で加圧しながら、0.057ItAで4.25Vまで充電した。 5) In the third charging step, the lithium ion secondary battery was again sealed and charged to 4.25 V at 0.057 ItA while being pressurized at the same pressure as described above.
6)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 6) Pressurization to the secondary battery was released, and sealing was temporarily released to perform a gas exhaust process.
全ての工程が終了した後、16時間以内に満充電状態で解体し、目視検査および写真での記録を行った。これらの操作により電極群の充電状態およびセパレータの状態を調査した。結果を下記表1に示す。 After the completion of all the steps, it was disassembled in a fully charged state within 16 hours, and visual inspection and photography were recorded. By these operations, the charged state of the electrode group and the state of the separator were investigated. The results are shown in Table 1 below.
(実施例2)
実施例1と同様な工程を経た密閉状態のリチウムイオン二次電池を下記条件にて初回充電した。
(Example 2)
A sealed lithium ion secondary battery that had undergone the same steps as in Example 1 was charged for the first time under the following conditions.
1)1回目の充電工程は加圧状態を維持しながら、0.01ItAで2時間を行った。 1) The first charging step was performed at 0.01 ItA for 2 hours while maintaining the pressurized state.
2)1回目の充電工程後、加圧状態を維持しながら、16時間の静置を行った。 2) After the 1st charge process, it left still for 16 hours, maintaining a pressurization state.
3)2回目の充電工程は加圧状態を維持しながら、0.057ItAで8.4時間行った。2回目の充電工程までの充電電気量は、定格容量の50%とした。 3) The second charging step was carried out at 0.057 ItA for 8.4 hours while maintaining the pressurized state. The amount of electricity charged until the second charging step was 50% of the rated capacity.
4)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 4) The gas exhaust process was performed by releasing the pressure applied to the secondary battery and further temporarily releasing the sealing.
5)3回目の充電工程は、リチウムイオン二次電池を再度、密閉状態にし、前記と同じ圧力で加圧しながら、0.057ItAで4.25Vまで充電した。 5) In the third charging step, the lithium ion secondary battery was again sealed and charged to 4.25 V at 0.057 ItA while being pressurized at the same pressure as described above.
実施例1と同様な方法により電極群の充電状態およびセパレータの状態を調査した結果を下記表1に示す。 The results of investigating the charged state of the electrode group and the state of the separator by the same method as in Example 1 are shown in Table 1 below.
(実施例3)
実施例1と同様な工程を経た密閉状態のリチウムイオン二次電池を下記条件にて初回充電した。
(Example 3)
A sealed lithium ion secondary battery that had undergone the same steps as in Example 1 was charged for the first time under the following conditions.
1)1回目の充電工程は加圧状態を維持しながら、0.01ItAで2時間を行った。 1) The first charging step was performed at 0.01 ItA for 2 hours while maintaining the pressurized state.
2)1回目の充電工程後、加圧状態を維持しながら、16時間の静置を行った。 2) After the 1st charge process, it left still for 16 hours, maintaining a pressurization state.
3)2回目の充電工程は加圧状態を維持しながら、0.057ItAで6.7時間行った。2回目の充電工程までの充電電気量は、定格容量の40%とした。 3) The second charging step was performed for 6.7 hours at 0.057 ItA while maintaining the pressurized state. The amount of electricity charged until the second charging step was 40% of the rated capacity.
4)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 4) The gas exhaust process was performed by releasing the pressure applied to the secondary battery and further temporarily releasing the sealing.
5)3回目の充電工程は、リチウムイオン二次電池を再度、密閉状態にし、前記と同じ圧力で加圧しながら、0.057ItAで4.25Vまで充電した。 5) In the third charging step, the lithium ion secondary battery was again sealed and charged to 4.25 V at 0.057 ItA while being pressurized at the same pressure as described above.
実施例1と同様な方法により電極群の充電状態およびセパレータの状態を調査した結果を下記表1に示す。 The results of investigating the charged state of the electrode group and the state of the separator by the same method as in Example 1 are shown in Table 1 below.
(実施例4)
実施例1と同様な工程を経た密閉状態のリチウムイオン二次電池を下記条件にて初回充電した。
Example 4
A sealed lithium ion secondary battery that had undergone the same steps as in Example 1 was charged for the first time under the following conditions.
1)1回目の充電工程は加圧状態を維持しながら、0.01ItAで2時間を行った。 1) The first charging step was performed at 0.01 ItA for 2 hours while maintaining the pressurized state.
2)1回目の充電工程後、加圧状態を維持しながら、16時間の静置を行った。 2) After the 1st charge process, it left still for 16 hours, maintaining a pressurization state.
3)2回目の充電工程は加圧状態を維持しながら、0.057ItAで10.2時間行った。2回目の充電工程までの充電電気量は、定格容量の60%とした。 3) The second charging step was performed at 0.057 ItA for 10.2 hours while maintaining the pressurized state. The amount of electricity charged until the second charging step was 60% of the rated capacity.
4)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 4) The gas exhaust process was performed by releasing the pressure applied to the secondary battery and further temporarily releasing the sealing.
5)3回目の充電工程は、リチウムイオン二次電池を再度、密閉状態にし、前記と同じ圧力で加圧しながら、0.057ItAで4.25Vまで充電した。 5) In the third charging step, the lithium ion secondary battery was again sealed and charged to 4.25 V at 0.057 ItA while being pressurized at the same pressure as described above.
実施例1と同様な方法により電極群の充電状態およびセパレータの状態を調査した結果を下記表1に示す。 The results of investigating the charged state of the electrode group and the state of the separator by the same method as in Example 1 are shown in Table 1 below.
(実施例5)
実施例1と同様な工程を経た密閉状態のリチウムイオン二次電池を下記条件にて初回充電した。
(Example 5)
A sealed lithium ion secondary battery that had undergone the same steps as in Example 1 was charged for the first time under the following conditions.
1)1回目の充電工程は加圧状態を維持しながら、0.01ItAで2時間を行った。 1) The first charging step was performed at 0.01 ItA for 2 hours while maintaining the pressurized state.
2)1回目の充電工程後、加圧状態を維持しながら、16時間の静置を行った。 2) After the 1st charge process, it left still for 16 hours, maintaining a pressurization state.
3)2回目の充電工程は加圧状態を維持しながら、0.057ItAで13.7時間行った。2回目の充電工程までの充電電気量は、定格容量の80%とした。 3) The second charging step was performed at 0.057 ItA for 13.7 hours while maintaining the pressurized state. The amount of electricity charged until the second charging step was 80% of the rated capacity.
4)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 4) The gas exhaust process was performed by releasing the pressure applied to the secondary battery and further temporarily releasing the sealing.
5)3回目の充電工程は、リチウムイオン二次電池を再度、密閉状態にし、前記と同じ圧力で加圧しながら、0.057ItAで4.25Vまで充電した。 5) In the third charging step, the lithium ion secondary battery was again sealed and charged to 4.25 V at 0.057 ItA while being pressurized at the same pressure as described above.
実施例1と同様な方法により電極群の充電状態およびセパレータの状態を調査した結果を下記表1に示す。 The results of investigating the charged state of the electrode group and the state of the separator by the same method as in Example 1 are shown in Table 1 below.
(比較例1)
実施例1と同様な工程を経た密閉状態のリチウムイオン二次電池を下記条件にて初回充電した。
(Comparative Example 1)
A sealed lithium ion secondary battery that had undergone the same steps as in Example 1 was charged for the first time under the following conditions.
1)1回目の充電工程は加圧状態を維持しながら、0.01ItAで2時間を行った。 1) The first charging step was performed at 0.01 ItA for 2 hours while maintaining the pressurized state.
2)1回目の充電工程後、加圧状態を維持しながら、16時間の静置を行った。 2) After the 1st charge process, it left still for 16 hours, maintaining a pressurization state.
3)2回目の充電工程は加圧状態を維持しながら、0.057ItAで8.4時間行った。2回目の充電工程までの充電電気量は、定格容量の50%とした。 3) The second charging step was carried out at 0.057 ItA for 8.4 hours while maintaining the pressurized state. The amount of electricity charged until the second charging step was 50% of the rated capacity.
4)ガス排気をせずに3回目の充電工程を実行した。3回目の充電工程は、加圧状態を維持しながら、0.057ItAで4.25Vまで充電した。 4) The third charging step was performed without exhausting the gas. In the third charging step, the battery was charged to 4.25 V at 0.057 ItA while maintaining the pressurized state.
5)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 5) Pressurization to the secondary battery was released, and further, the sealing was temporarily released to perform the gas exhaust process.
実施例1と同様な方法により電極群の充電状態およびセパレータの状態を調査した結果を下記表1に示す。 The results of investigating the charged state of the electrode group and the state of the separator by the same method as in Example 1 are shown in Table 1 below.
(比較例2)
実施例1と同様な工程を経た密閉状態のリチウムイオン二次電池を下記条件にて初回充電した。
(Comparative Example 2)
A sealed lithium ion secondary battery that had undergone the same steps as in Example 1 was charged for the first time under the following conditions.
1)1回目の充電工程は加圧状態を維持しながら、0.01ItAで2時間を行った。 1) The first charging step was performed at 0.01 ItA for 2 hours while maintaining the pressurized state.
2)静置及びガス排気を行わずに加圧状態を維持しながら、0.057ItAで4.25Vまで充電した。 2) It charged to 4.25V with 0.057 ItA, maintaining a pressurization state without performing stationary and gas exhaustion.
3)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 3) The pressure on the secondary battery was released, and the sealing was temporarily released to perform the gas exhaust process.
実施例1と同様な方法により電極群の充電状態およびセパレータの状態を調査した結果を下記表1に示す。 The results of investigating the charged state of the electrode group and the state of the separator by the same method as in Example 1 are shown in Table 1 below.
(比較例3)
実施例1と同様な工程を経た密閉状態のリチウムイオン二次電池を下記条件にて初回充電した。
(Comparative Example 3)
A sealed lithium ion secondary battery that had undergone the same steps as in Example 1 was charged for the first time under the following conditions.
1)1回目の充電工程は加圧状態を維持しながら、0.01ItAで2時間を行った。 1) The first charging step was performed at 0.01 ItA for 2 hours while maintaining the pressurized state.
2)静置せずに2回目の充電工程を実行した。2回目の充電工程は加圧状態を維持しながら、0.057ItAで8.4時間行った。2回目の充電工程までの充電電気量は、定格容量の50%とした。 2) The 2nd charge process was performed without leaving still. The second charging step was performed at 0.057 ItA for 8.4 hours while maintaining the pressurized state. The amount of electricity charged until the second charging step was 50% of the rated capacity.
3)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 3) The pressure on the secondary battery was released, and the sealing was temporarily released to perform the gas exhaust process.
4)3回目の充電工程は、リチウムイオン二次電池を再度、密閉状態にし、実施例1と同じ圧力で加圧しながら、0.057ItAで4.25Vまで充電した。 4) In the third charging step, the lithium ion secondary battery was again sealed and charged to 4.25 V at 0.057 ItA while being pressurized at the same pressure as in Example 1.
実施例1と同様な方法により電極群の充電状態およびセパレータの状態を調査した結果を下記表1に示す。 The results of investigating the charged state of the electrode group and the state of the separator by the same method as in Example 1 are shown in Table 1 below.
(比較例4)
1)1回目の充電工程は加圧状態を維持しながら、0.01ItAで2時間を行った。
(Comparative Example 4)
1) The first charging step was performed at 0.01 ItA for 2 hours while maintaining the pressurized state.
2)静置せずに2回目の充電工程を実行した。2回目の充電工程は加圧状態を維持しながら、0.057ItAで8.4時間行った。2回目の充電工程までの充電電気量は、定格容量の50%とした。 2) The 2nd charge process was performed without leaving still. The second charging step was performed at 0.057 ItA for 8.4 hours while maintaining the pressurized state. The amount of electricity charged until the second charging step was 50% of the rated capacity.
3)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 3) The pressure on the secondary battery was released, and the sealing was temporarily released to perform the gas exhaust process.
4)3回目の充電工程は、リチウムイオン二次電池を再度、密閉状態にし、実施例1と同じ圧力で加圧しながら、0.057ItAで4.25Vまで充電した。 4) In the third charging step, the lithium ion secondary battery was again sealed and charged to 4.25 V at 0.057 ItA while being pressurized at the same pressure as in Example 1.
5)二次電池への加圧を解除し、さらに封止を一時的に解除してガス排気工程を行った。 5) Pressurization to the secondary battery was released, and further, the sealing was temporarily released to perform the gas exhaust process.
実施例1と同様な方法により電極群の充電状態およびセパレータの状態を調査した結果を下記表1に示す。
前記表1から明らかなように電極群を収納した外装体内に非水電解液を注入した後、当該外装体を封止して密閉した状態で少なくとも2回の充電工程を含み、1回目の充電工程後に静置し、2回目の充電工程後にガス排気を行う実施例1〜5の初回充電は、電極群の充電状態が均一で、セパレータへの皺発生を防止できることがわかる。 As is apparent from Table 1, after the nonaqueous electrolyte is injected into the exterior body containing the electrode group, the exterior body is sealed and sealed, and includes at least two charging steps. It can be seen that the initial charging in Examples 1 to 5 where the process is left after the process and the gas is exhausted after the second charging process has a uniform charged state of the electrode group and can prevent generation of wrinkles on the separator.
これに対し、実施例1〜5の方法から外れる比較例1〜4の初回放電は電極群の充電状態が不均一になり、セパレータに皺が発生することがわかる。 On the other hand, in the first discharges of Comparative Examples 1 to 4 that deviate from the methods of Examples 1 to 5, it can be seen that the charged state of the electrode group becomes uneven and wrinkles are generated in the separator.
1…リチウム二次電池、2…外装体、3…積層電極群、4…正極、5…負極、6…セパレータ、41…正極集電体、42…正極層、51…負極集電体、52…負極層。
DESCRIPTION OF
Claims (4)
前記初回充電は、前記電極群を収納した前記外装体内に前記非水電解液を注入した後、当該外装体を封止して密閉した状態で少なくとも2回の充電工程を含み、
1回目の充電工程後に静置し、2回目の充電工程後にガス排気を行うことを特徴とするリチウムイオン二次電池の初回充電方法におけるセパレータ皺抑制方法。 Initial charging of a lithium ion secondary battery comprising: an exterior body; an electrode group that is housed in the exterior body, and alternately stacks positive and negative electrodes with a separator interposed therebetween; and a non-aqueous electrolyte contained in the exterior body A separator wrinkle suppression method in the method,
The initial charging includes at least two charging steps in a state where the outer body is sealed and sealed after injecting the non-aqueous electrolyte into the outer body housing the electrode group,
A separator soot suppression method in an initial charging method of a lithium ion secondary battery, wherein the method is left after the first charging step and gas is exhausted after the second charging step.
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