JPH11297357A - Method for producing polymer lithium ion secondary battery - Google Patents
Method for producing polymer lithium ion secondary batteryInfo
- Publication number
- JPH11297357A JPH11297357A JP10094200A JP9420098A JPH11297357A JP H11297357 A JPH11297357 A JP H11297357A JP 10094200 A JP10094200 A JP 10094200A JP 9420098 A JP9420098 A JP 9420098A JP H11297357 A JPH11297357 A JP H11297357A
- Authority
- JP
- Japan
- Prior art keywords
- electrode mixture
- positive electrode
- negative electrode
- lithium ion
- secondary battery
- Prior art date
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Classifications
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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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- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
(57)【要約】
【課題】 ゲル化によって正極合剤や負極合剤の組成に
大きな変動をきたすことなく、良好な電池性能を有する
ポリマーリチウムイオン二次電池を安定して製造する方
法を提供する。
【解決手段】 集電体の少なくとも一方の面にゲル状の
正極合剤層を形成してなるシート状の正極、集電体の少
なくとも一方の面にゲル状の負極合剤層を形成してなる
シート状の負極およびシート状のポリマー電解質層を有
するポリマーリチウムイオン二次電池の製造方法にあた
り、上記正極合剤および負極合剤におけるゲル化剤とし
てポリフッ化ビニリデンを用い、かつ電解質成分として
プロピレンカーボネートを電解液溶媒として含む電解液
を用い、上記正極合剤および負極合剤をゲル化する際に
90〜120℃でゲル化する。PROBLEM TO BE SOLVED: To provide a method for stably producing a polymer lithium ion secondary battery having good battery performance without causing a great change in the composition of a positive electrode mixture and a negative electrode mixture due to gelation. I do. SOLUTION: A sheet-like positive electrode in which a gel-like positive electrode mixture layer is formed on at least one surface of a current collector, and a gel-like negative electrode mixture layer is formed on at least one surface of a current collector. In the method for producing a polymer lithium ion secondary battery having a sheet-shaped negative electrode and a sheet-shaped polymer electrolyte layer, polyvinylidene fluoride is used as a gelling agent in the positive electrode mixture and the negative electrode mixture, and propylene carbonate is used as an electrolyte component. Is used at the temperature of 90 to 120 ° C. when the positive electrode mixture and the negative electrode mixture are gelled by using an electrolytic solution containing as an electrolyte solvent.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ポリマーリチウム
イオン二次電池の製造方法に関し、さらに詳しくは、良
好な電池性能を有するポリマーリチウムイオン二次電池
を安定して製造することができるポリマーリチウムイオ
ン二次電池の製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polymer lithium ion secondary battery, and more particularly, to a method for producing a polymer lithium ion secondary battery having good battery performance. The present invention relates to a method for manufacturing a secondary battery.
【0002】[0002]
【従来の技術】従来より、電解質を固体化すると漏液の
心配のない電池が得られることから、究極の電池と目さ
れていたが、イオン伝導度が溶液系のものに比べて数桁
低いなどの問題があったため、汎用性のある電池の出現
までには至らなかった。2. Description of the Related Art Conventionally, when an electrolyte is solidified, a battery free from liquid leakage can be obtained. Therefore, the battery has been regarded as the ultimate battery. However, the ion conductivity is several orders of magnitude lower than that of a solution type. Due to such problems, it did not reach the appearance of a versatile battery.
【0003】ところが、近年になってポリマーを有機溶
媒系の電解液とともにゲル化させると、イオン伝導度が
10-3S/cm程度に向上したイオン伝導度の高いポリ
マー電解質が得られるようになり、これを電池の電解質
として使用することにより特性の良い電池が得られるよ
うになったことから、ポリマー電池が再び脚光を浴びる
ようになってきた。However, in recent years, when a polymer is gelled together with an organic solvent-based electrolyte, a polymer electrolyte having a high ionic conductivity and an improved ionic conductivity of about 10 −3 S / cm can be obtained. By using this as an electrolyte of a battery, a battery having good characteristics has been obtained, and thus polymer batteries have come into the spotlight again.
【0004】[0004]
【発明が解決しようとする課題】このようなポリマーリ
チウムイオン二次電池において、正極や負極の作製に際
してのゲル化は、正極、負極の活物質、電解液、ゲル化
剤などを混合して調製したペースト状の電極合剤を集電
体に塗布したのち加熱することによって行われるが、加
熱温度が電解液溶媒の蒸発する領域にあるため、加熱温
度の適否は正負極の組成の良否に影響を及ぼし、良好な
性能を有する電池が得られない原因になる場合があっ
た。In such a polymer lithium ion secondary battery, gelation at the time of manufacturing a positive electrode or a negative electrode is performed by mixing an active material of the positive electrode, the negative electrode, an electrolytic solution, a gelling agent, and the like. It is performed by applying the paste-like electrode mixture to the current collector and heating it.However, since the heating temperature is in the area where the electrolyte solvent evaporates, the appropriateness of the heating temperature affects the quality of the positive and negative electrode compositions. In some cases, resulting in failure to obtain a battery having good performance.
【0005】従って、本発明は、上記のような従来技術
の問題点を解決し、良好な電池性能を有するポリマーリ
チウムイオン二次電池を安定して製造する方法を提供す
ることを目的とする。Accordingly, an object of the present invention is to solve the above-mentioned problems of the prior art and to provide a method for stably producing a polymer lithium ion secondary battery having good battery performance.
【0006】[0006]
【課題を解決するための手段】本発明者らは、上記課題
を解決するために、示差熱・熱天秤分析および電池試験
などを駆使して鋭意研究を重ねた結果、正極合剤および
負極合剤におけるゲル化剤としてポリフッ化ビニリデン
を用い、かつ電解質成分としてプロピレンカーボネート
を電解液溶媒として含む電解液を用い、正極合剤および
負極合剤のゲル化を90〜120℃で行うときは、良好
な電池性能を有するポリマーリチウムイオン二次電池が
安定して得られることを見出し、本発明を完成するにい
たった。Means for Solving the Problems In order to solve the above-mentioned problems, the present inventors have conducted intensive studies using differential thermal / thermal balance analysis and battery tests, and as a result, the positive electrode mixture and the negative electrode mixture have been obtained. When using polyvinylidene fluoride as a gelling agent in the agent, and using an electrolyte containing propylene carbonate as an electrolyte solvent as an electrolyte component, and performing gelation of the positive electrode mixture and the negative electrode mixture at 90 to 120 ° C., The present inventors have found that a polymer lithium ion secondary battery having excellent battery performance can be stably obtained, and have completed the present invention.
【0007】すなわち、正極活物質のLiCoO2 や負
極活物質の黒鉛、導電材のアセチレンブラックなどは、
上記温度領域では分解したり、変化することはないが、
電解液溶媒のプロピレンカーボネートなどは上記温度領
域で蒸発が始まり、温度が120℃より高くなるとその
蒸発の度合がさらに加速する。That is, LiCoO 2 as a positive electrode active material, graphite as a negative electrode active material, acetylene black as a conductive material, etc.
It does not decompose or change in the above temperature range,
Evaporation of propylene carbonate or the like as an electrolyte solvent starts in the above temperature range, and when the temperature is higher than 120 ° C., the degree of the evaporation is further accelerated.
【0008】一方、ゲル化剤のポリフッ化ビニリデンは
90℃付近にゲル化点があり、150℃付近には融点が
存在している。従って、温度が90℃より低い場合は、
ゲル化が不充分であり、120℃より高くなると、前記
のように電解液溶媒が急激に蒸発するため、正極、負極
の組成が一定しなくなる。On the other hand, polyvinylidene fluoride as a gelling agent has a gel point around 90 ° C. and a melting point around 150 ° C. Therefore, if the temperature is lower than 90 ° C,
If the gelation is insufficient and the temperature is higher than 120 ° C., the composition of the positive electrode and the negative electrode becomes unstable because the electrolyte solvent evaporates rapidly as described above.
【0009】従って、本発明では、上記のような90〜
120℃の温度条件下でゲル化を行うことにより均一な
組成のゲル状正極合剤およびゲル状負極合剤を安定して
得ることが可能になり、良好な電池性能を有するポリマ
ーリチウムイオン二次電池を安定して製造することがで
きる。Therefore, according to the present invention, 90-
By performing gelation under a temperature condition of 120 ° C., it is possible to stably obtain a gelled positive electrode mixture and a gelled negative electrode mixture having a uniform composition, and a polymer lithium ion secondary battery having good battery performance A battery can be manufactured stably.
【0010】これを図1を参照しつつ説明する。図1
は、プロピレンカーボネートおよびポリフッ化ビニリデ
ンを含む正極合剤の示差熱・熱天秤分析の結果を示した
ものである。図1より明らかなように、ポリフッ化ビニ
リデンのゲル化に伴う発熱は85℃付近で生じ、融解に
伴う吸熱が160〜170℃付近で生じることがわか
る。また、プロピレンカーボネートの蒸発に伴う減量は
80℃ぐらいから既に始まっており、200℃付近で減
量は終了する。プロピレンカーボネートの減量は温度が
上昇するに伴ってその減量速度が速くなることが図1よ
り明らかであり、120℃より高くなるとその度合いは
大きくなる。従って、ゲル化をでき、かつプロピレンカ
ーボネートの蒸発を極力押えることができる領域は90
℃〜120℃付近であることが図1より明かである。This will be described with reference to FIG. FIG.
Fig. 2 shows the results of differential thermal and thermobalance analysis of a positive electrode mixture containing propylene carbonate and polyvinylidene fluoride. As is clear from FIG. 1, it is found that the heat generation accompanying the gelation of polyvinylidene fluoride occurs at around 85 ° C., and the heat absorption accompanying the melting occurs at around 160 to 170 ° C. Further, the weight loss due to the evaporation of propylene carbonate has already started at about 80 ° C., and ends at about 200 ° C. It is apparent from FIG. 1 that the rate of weight loss of propylene carbonate increases as the temperature increases, and the degree of weight loss increases with the temperature higher than 120 ° C. Therefore, a region where gelation can be performed and evaporation of propylene carbonate can be suppressed as much as possible is 90%.
It is clear from FIG.
【0011】事実、60℃、90℃、110℃、120
℃、150℃の各温度でゲル化すればその効果の差は顕
著に現れる。すなわち、60℃でゲル化を試みると温度
が不充分であるため充分なゲル化をすることができな
い。150℃でのゲル化は電解液溶媒の蒸発により活物
質の乾燥が生じ、ゲル化時間が長くなるほどその乾燥は
より促進される。また、150℃でのゲル化は速く、均
一な温度コントロールが難しい。これに対し、90〜1
20℃でのゲル化はコントロールが可能で均一にゲル化
した正極合剤および負極合剤を得ることができる。In fact, 60 ° C., 90 ° C., 110 ° C., 120
If the gelation occurs at each temperature of 150 ° C. and 150 ° C., the difference in the effect becomes remarkable. That is, if gelation is attempted at 60 ° C., sufficient temperature cannot be obtained because the temperature is insufficient. Gelation at 150 ° C. causes drying of the active material due to evaporation of the electrolyte solvent, and the longer the gelation time, the more the drying is accelerated. Further, gelation at 150 ° C. is fast, and uniform temperature control is difficult. In contrast, 90-1
The gelation at 20 ° C. is controllable, and a uniformly gelled positive electrode mixture and negative electrode mixture can be obtained.
【0012】[0012]
【実施例】つぎに、実施例を挙げて本発明をより具体的
に説明する。ただし、本発明はそれらの実施例のみに限
定されるものではない。Next, the present invention will be described more specifically with reference to examples. However, the present invention is not limited to only these examples.
【0013】正極での実施例 正極活物質であるLiCoO2 10gに、導伝材のアセ
チレンブラック2g、プロピレンカーボネートを電解液
溶媒として含む電解液6gおよびポリフッ化ビニリデン
1.2gを加え、混合してペースト状の正極合剤を調製
した。上記電解液はプロピレンカーボネートとエチレン
カーボネートとの体積比1:1の混合溶媒にLiPF6
を1.22モル/リットル溶解させて調製したものであ
る。Examples for Positive Electrode To 10 g of LiCoO 2 as a positive electrode active material, 2 g of acetylene black as a conductive material, 6 g of an electrolytic solution containing propylene carbonate as an electrolytic solvent and 1.2 g of polyvinylidene fluoride were added and mixed. A paste-like positive electrode mixture was prepared. The electrolytic solution was prepared by mixing LiPF 6 in a mixed solvent of propylene carbonate and ethylene carbonate at a volume ratio of 1: 1.
Was dissolved in 1.22 mol / l.
【0014】このペースト状の正極合剤を集電体として
のアルミニウム箔の一方の面に塗布し、60℃、90
℃、110℃、120℃、150℃の各温度で10分間
それぞれ加熱した。その結果を下記の表1に示す。ま
た、それらを正極として用いた場合の電池性能を調べ、
その結果も表1に示した。電池は上記シート状の正極
と、負極活物質であるコークス6gに、導伝材のアセチ
レンブラック0.6g、正極に使用したものと同様のプ
ロピレンカーボネートを電解液溶媒として含む電解液5
gおよびポリフッ化ビニリデン0.8gを加えて混合し
てペースト状の負極合剤を調製し、このペースト状の負
極合剤を銅箔の一方の面に塗布し、120℃で加熱して
ゲル化させて得られたシート状の負極と、トリ(エチレ
ングリコール)ジメタクリレートとエチレングリコール
エチルカーボネートメタクリレートと2−エトキシアク
リレートとからなるアクリル系モノマー混合物、その重
合開始剤である過酸化ベンゾイルおよびプロピレンカー
ボネートを電解液溶媒として含む前記と同様の電解液の
混合物を加熱してモノマーを重合させるとともにゲル化
させることにより得られたシート状のゲル状電解質とを
組み合わせて構成したものであり、その電池性能の比較
は、20℃、0.5CでCCCVで4.2Vまで充電
し、0.5CでCVで2.75Vまで放電し、そのサイ
クル特性を比較することによって行った。This paste-like positive electrode mixture is applied to one surface of an aluminum foil as a current collector,
It heated at each temperature of 110 degreeC, 120 degreeC, and 150 degreeC for 10 minutes, respectively. The results are shown in Table 1 below. In addition, the battery performance when using them as the positive electrode was investigated,
The results are also shown in Table 1. The battery was composed of the above sheet-shaped positive electrode, 6 g of coke as a negative electrode active material, 0.6 g of acetylene black as a conductive material, and an electrolytic solution 5 containing the same propylene carbonate as that used for the positive electrode as an electrolytic solution solvent.
g and 0.8 g of polyvinylidene fluoride are added and mixed to prepare a paste-like negative electrode mixture, and this paste-like negative electrode mixture is applied to one surface of a copper foil and gelled by heating at 120 ° C. A sheet-like negative electrode obtained by the above, an acrylic monomer mixture composed of tri (ethylene glycol) dimethacrylate, ethylene glycol ethyl carbonate methacrylate and 2-ethoxyacrylate, and benzoyl peroxide and propylene carbonate as polymerization initiators thereof It is a combination of a sheet-like gel electrolyte obtained by heating a mixture of the same electrolyte solution as described above containing as an electrolyte solvent, and polymerizing the monomer and gelling the mixture. For comparison, charge at 20 ° C, CCCV to 4.2V at 0.5C, and CV at 0.5C. Discharged to 2.75 V, it was carried out by comparing the cycle characteristics.
【0015】[0015]
【表1】 [Table 1]
【0016】負極での実施例 負極活物質であるコークス6gに、導伝材のアセチレン
ブラック0.6g、前記正極に使用したものと同様のプ
ロピレンカーボネートを電解液溶媒として含む電解液5
gおよびポリフッ化ビニリデン0.8gを加え、混合し
てペースト状の負極合剤を調製した。Example of Negative Electrode An electrolytic solution containing 6 g of coke as the negative electrode active material, 0.6 g of acetylene black as a conductive material, and propylene carbonate similar to that used for the positive electrode as an electrolytic solution solvent.
g and 0.8 g of polyvinylidene fluoride were added and mixed to prepare a paste-like negative electrode mixture.
【0017】このペースト状の負極合剤を集電体として
の銅箔の一方の面に塗布し、60℃、90℃、110
℃、120℃、150℃の各温度で10分間それぞれ加
熱した。その結果を下記の表2に示す。また、それらを
負極として用いた場合の電池性能を調べ、その結果も表
2に示した。電池は上記シート状の負極と、正極活物質
であるLiCoO2 10gに、導伝材のアセチレンブラ
ック2g、プロピレンカーボネートを電解液溶媒として
含む前記と同様の電解液6gおよびポリフッ化ビニリデ
ン1.2gを加えて混合してペースト状の正極合剤を調
製し、このペースト状の正極合剤をアルミニウム箔の一
方の面に塗布し、120℃で加熱してゲル化させること
により得られたシート状の正極と、トリ(エチレングリ
コール)ジメタクリレートとエチレングリコールエチル
カーボネートメタクリレートと2−エトキシアクリレー
トとからなるアクリル系モノマー混合物、その重合開始
剤である過酸化ベンゾイルおよびプロピレンカーボネー
トを電解液溶媒として含む前記と同様の電解液の混合物
を加熱してモノマーを重合させるとともにゲル化させる
ことにより得られたシート状のゲル状電解質とを組み合
わせて構成したものであり、その電池性能の比較は、2
0℃、0.5CでCCCVで4.2Vまで充電し、0.
5CでCVで2.75Vまで放電し、そのサイクル特性
を比較することによって行った。This paste-like negative electrode mixture is applied to one surface of a copper foil as a current collector,
It heated at each temperature of 120 degreeC, 120 degreeC, and 150 degreeC for 10 minutes, respectively. The results are shown in Table 2 below. Further, the battery performance when these were used as the negative electrode was examined, and the results are also shown in Table 2. In the battery, the above sheet-shaped negative electrode, 10 g of LiCoO 2 as a positive electrode active material, 2 g of acetylene black as a conductive material, 6 g of the same electrolytic solution containing propylene carbonate as an electrolytic solvent, and 1.2 g of polyvinylidene fluoride were used. A paste-like positive electrode mixture is prepared by adding and mixing, and the paste-like positive electrode mixture is applied to one surface of an aluminum foil, and heated at 120 ° C. to be gelled to obtain a sheet-like positive electrode mixture. A positive electrode, an acrylic monomer mixture composed of tri (ethylene glycol) dimethacrylate, ethylene glycol ethyl carbonate methacrylate and 2-ethoxy acrylate, and benzoyl peroxide and propylene carbonate, which are polymerization initiators thereof, as described above containing an electrolyte solvent Heating the mixture of electrolytes to polymerize the monomers Together are those formed by combining the obtained sheet-shaped gel electrolyte by gelling, comparison of the cell performance, 2
The battery was charged to 4.2 V by CCCV at 0.5 ° C. at 0 ° C.
This was performed by discharging the battery to CV at 2.75 V at 5 C and comparing the cycle characteristics.
【0018】[0018]
【表2】 [Table 2]
【0019】表1および表2に示す結果から明らかなよ
うに、ゲル化温度が低すぎる場合は、ゲル化が充分に行
えず、そのため、電極と集電体との密着性が不充分にな
り、電極の集電体からの剥離が生じて、電池性能が出
ず、また、ゲル化温度が高すぎる場合は、電解液溶媒で
あるプロピレンカーボネートなどの蒸発を招いて、活物
質などの乾燥が生じ、その結果、イオンの伝導が不充分
になって、充放電が不可能になった。As is evident from the results shown in Tables 1 and 2, when the gelation temperature is too low, gelation cannot be performed sufficiently, so that the adhesion between the electrode and the current collector becomes insufficient. If the electrode is peeled off from the current collector and the battery performance is not obtained, and if the gelling temperature is too high, evaporation of the electrolyte solvent such as propylene carbonate is caused, and drying of the active material and the like occurs. As a result, the conduction of ions became insufficient, and charging and discharging became impossible.
【0020】[0020]
【発明の効果】以上説明したように、本発明では、正極
合剤および負極合剤のゲル化を90〜120℃で行うこ
とによって、良好な電池性能を有するポリマーリチウム
イオン二次電池を提供することができた。As described above, the present invention provides a polymer lithium ion secondary battery having good battery performance by gelling the positive electrode mixture and the negative electrode mixture at 90 to 120 ° C. I was able to.
【0021】また、本発明によれば、ゲル化によって正
極合剤や負極合剤の組成に大きな変動をきたすことがな
いので、良好な電池性能を有するポリマーリチウムイオ
ン二次電池を安定して製造することができる。Further, according to the present invention, since the composition of the positive electrode mixture and the negative electrode mixture does not greatly change due to gelation, a polymer lithium ion secondary battery having good battery performance can be stably manufactured. can do.
【図1】正極合剤を示差熱分析および熱天秤分析した結
果を示す図である。FIG. 1 is a diagram showing the results of differential thermal analysis and thermobalance analysis of a positive electrode mixture.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 横山 映理 大阪府茨木市丑寅一丁目1番88号 日立マ クセル株式会社内 (72)発明者 杉山 拓 大阪府茨木市丑寅一丁目1番88号 日立マ クセル株式会社内 (72)発明者 川合 徹夫 大阪府茨木市丑寅一丁目1番88号 日立マ クセル株式会社内 ──────────────────────────────────────────────────の Continuing on the front page (72) Inventor Eri Yokoyama 1-88 Ushitora, Ibaraki City, Osaka Prefecture Inside Hitachi Maxell Co., Ltd. (72) Inventor Taku Sugiyama 1-88 Ushitora, Ibaraki City, Osaka Prefecture Hitachi Maxell Co., Ltd. (72) Inventor Tetsuo Kawai 1-88 Ushitora, Ibaraki-shi, Osaka Hitachi Maxell Co., Ltd.
Claims (1)
正極合剤層を形成してなるシート状の正極、集電体の少
なくとも一方の面にゲル状の負極合剤層を形成してなる
シート状の負極およびシート状のポリマー電解質層を有
するポリマーリチウムイオン二次電池の製造方法にあた
り、上記正極合剤および負極合剤におけるゲル化剤とし
てポリフッ化ビニリデンを用い、かつ電解質成分として
プロピレンカーボネートを電解液溶媒として含む電解液
を用い、上記正極合剤および負極合剤をゲル化する際に
90〜120℃でゲル化することを特徴とするポリマー
リチウムイオン二次電池の製造方法。1. A sheet-like positive electrode in which a gel-like positive electrode mixture layer is formed on at least one surface of a current collector, and a gel-like negative electrode mixture layer is formed on at least one surface of a current collector. In a method for producing a polymer lithium ion secondary battery having a sheet-shaped negative electrode and a sheet-shaped polymer electrolyte layer, polyvinylidene fluoride is used as a gelling agent in the positive electrode mixture and the negative electrode mixture, and propylene is used as an electrolyte component. A method for producing a polymer lithium ion secondary battery, comprising using an electrolytic solution containing carbonate as an electrolytic solution solvent and gelling the positive electrode mixture and the negative electrode mixture at 90 to 120 ° C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10094200A JPH11297357A (en) | 1998-04-07 | 1998-04-07 | Method for producing polymer lithium ion secondary battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10094200A JPH11297357A (en) | 1998-04-07 | 1998-04-07 | Method for producing polymer lithium ion secondary battery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH11297357A true JPH11297357A (en) | 1999-10-29 |
Family
ID=14103665
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10094200A Withdrawn JPH11297357A (en) | 1998-04-07 | 1998-04-07 | Method for producing polymer lithium ion secondary battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH11297357A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003022840A (en) * | 2001-07-09 | 2003-01-24 | Toyota Motor Corp | Lithium secondary battery |
| WO2015151145A1 (en) * | 2014-03-31 | 2015-10-08 | 株式会社日立製作所 | All-solid lithium secondary cell |
| JP2019212619A (en) * | 2018-05-30 | 2019-12-12 | 三洋化成工業株式会社 | Manufacturing method of electrode active material layer, manufacturing method of electrode for lithium ion battery, and manufacturing method for lithium ion battery |
| US11777145B2 (en) | 2020-06-24 | 2023-10-03 | Corning Incorporated | Gel composite cathode for solid-state batteries and methods of manufacturing thereof |
| GB2621116A (en) * | 2022-07-29 | 2024-02-07 | Dyson Technology Ltd | Electrode precursor composition |
-
1998
- 1998-04-07 JP JP10094200A patent/JPH11297357A/en not_active Withdrawn
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003022840A (en) * | 2001-07-09 | 2003-01-24 | Toyota Motor Corp | Lithium secondary battery |
| WO2015151145A1 (en) * | 2014-03-31 | 2015-10-08 | 株式会社日立製作所 | All-solid lithium secondary cell |
| JP2019212619A (en) * | 2018-05-30 | 2019-12-12 | 三洋化成工業株式会社 | Manufacturing method of electrode active material layer, manufacturing method of electrode for lithium ion battery, and manufacturing method for lithium ion battery |
| US11777145B2 (en) | 2020-06-24 | 2023-10-03 | Corning Incorporated | Gel composite cathode for solid-state batteries and methods of manufacturing thereof |
| GB2621116A (en) * | 2022-07-29 | 2024-02-07 | Dyson Technology Ltd | Electrode precursor composition |
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