JP2000311710A - Solid electrolyte battery and method of manufacturing the same - Google Patents
Solid electrolyte battery and method of manufacturing the sameInfo
- Publication number
- JP2000311710A JP2000311710A JP11120381A JP12038199A JP2000311710A JP 2000311710 A JP2000311710 A JP 2000311710A JP 11120381 A JP11120381 A JP 11120381A JP 12038199 A JP12038199 A JP 12038199A JP 2000311710 A JP2000311710 A JP 2000311710A
- Authority
- JP
- Japan
- Prior art keywords
- solid electrolyte
- active material
- battery
- electrode active
- positive electrode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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Classifications
-
- 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
-
- 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
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
(57)【要約】
【課題】 電池としての充放電のレート特性や保存性な
どの諸特性が向上した、特に電解液を全く含まない二次
電池としてサイクル特性に優れたエネルギー密度の高い
固体電解質電池を提供することを目的とする。
【解決手段】 正極活物質と負極活物質から成る一対の
電極間に固体電解質を介在させてなる固体電解質電池に
おいて、前記固体電解質と同じ材料から成る無機酸化物
が前記正極活物質あるいは負極活物質の粒子間で三次元
ネットワーク構造を構成するように前記正極活物質ある
いは負極活物質の粒子間に、介在させた。
PROBLEM TO BE SOLVED: To improve a charge / discharge rate characteristic and a storage property of a battery, and to improve a cycle characteristic as a secondary battery containing no electrolytic solution at all, particularly a solid electrolyte having a high energy density. It is intended to provide a battery. SOLUTION: In a solid electrolyte battery in which a solid electrolyte is interposed between a pair of electrodes composed of a positive electrode active material and a negative electrode active material, an inorganic oxide made of the same material as the solid electrolyte is used as the positive electrode active material or the negative electrode active material. Were interposed between the particles of the positive electrode active material or the negative electrode active material so as to form a three-dimensional network structure.
Description
【0001】[0001]
【発明の属する技術分野】本発明は無機酸化物から成る
固体電解質を用いた固体電解質電池に関する。The present invention relates to a solid electrolyte battery using a solid electrolyte made of an inorganic oxide.
【0002】[0002]
【従来の技術および発明が解決しようとする課題】従来
から各種電池には水系あるいは非水系の液状の電解質が
使用されていたが、近年、ビデオ撮影装置、ノートパソ
コン、あるいは携帯電話などの携帯用情報端末機器に代
表される各種電子応用機器の薄型かつ軽量小型化の要求
に伴い、液状の電解質に代えて高分子材料から成る固体
状の電解質を用いた固体電解質電池が注目されている。2. Description of the Related Art Conventionally, aqueous or non-aqueous liquid electrolytes have been used for various types of batteries. Recently, however, portable batteries such as video photographing devices, notebook computers, and mobile phones have been used. 2. Description of the Related Art Along with a demand for thin, lightweight, and miniaturized electronic application devices represented by information terminal devices, a solid electrolyte battery using a solid electrolyte made of a polymer material instead of a liquid electrolyte has attracted attention.
【0003】かかる固体電解質電池は電解質が液状でな
いため、電池の発火などを誘引する漏液の心配がなく、
腐食性も小さいという特徴を有する。しかしながら、こ
のような高分子材料から成る固体電解質を例えば二次電
池の電解質として用いた場合には、この高分子材料のイ
オン伝導性が低いため、大電流を取り出せず、また充放
電におけるレート特性やサイクル特性、あるいは保存特
性などの電池性能が悪いという問題があった。[0003] In such a solid electrolyte battery, since the electrolyte is not liquid, there is no need to worry about leakage of liquid which may cause ignition of the battery.
It has the characteristic of low corrosiveness. However, when a solid electrolyte made of such a polymer material is used as, for example, an electrolyte for a secondary battery, a large current cannot be taken out due to the low ionic conductivity of the polymer material, and the rate characteristics in charge / discharge. There is a problem that battery performance such as battery characteristics, cycle characteristics, and storage characteristics is poor.
【0004】このような問題を解決するために、高分子
材料中に金属酸化物や電子電導性微粒子を添加分散した
固体電解質を形成して活物質の利用率の向上を図ろうと
するもの(例えば特開平5−314995号、特開平5
−315008号、特開平5−074466号)、ある
いは高分子の網目状構造をイオン伝導経路とするもの
(特開平5−325990号)などが提案されている。In order to solve such a problem, an attempt is made to improve the utilization rate of an active material by forming a solid electrolyte in which a metal oxide or electron-conductive fine particles are added and dispersed in a polymer material (for example, a solid electrolyte). JP-A-5-314995, JP-A-5-314995
JP-A-315008, JP-A-5-07466, and those using a polymer network structure as an ion conduction path (JP-A-5-325990) have been proposed.
【0005】しかしながら、これらの電池でも有機電解
液を取り込まない限り、良好なイオン伝導性を確保でき
ず、固体電解質が目的とする電極反応において良イオン
伝導体としての役割を十分に果たすことができないもの
であった。However, even in these batteries, unless the organic electrolyte is taken in, good ionic conductivity cannot be ensured, and the solid electrolyte cannot sufficiently play a role as a good ionic conductor in a target electrode reaction. Was something.
【0006】したがって、これらの各手法を固体電解質
電池に適用したとしても、イオン伝導度は従来の液状の
電解質に比べて数段低く、固体電解質電池としての有効
性は不十分である。しかも、充放電サイクルの履歴によ
って固体電解質と活物質との界面や固体電解質粒子間の
界面でのイオンのトラップが起こり、充放電可能な容量
が短期間に低下してサイクル特性の劣化を引き起こすな
どの問題があった。Therefore, even if each of these techniques is applied to a solid electrolyte battery, the ionic conductivity is several steps lower than that of a conventional liquid electrolyte, and the effectiveness as a solid electrolyte battery is insufficient. In addition, the charge / discharge cycle history causes ions to be trapped at the interface between the solid electrolyte and the active material and at the interface between the solid electrolyte particles. There was a problem.
【0007】一般に、全固体二次電池では、固体電解質
内のイオン伝導が速やかに行われることで電池の性能向
上が図れるため、固体電解質はその内部にイオン伝導を
阻害する欠陥が少ないものほど良イオン伝導体となっ
て、充放電の性能が向上するものである。しかしなが
ら、前記提案では固体電解質そのものの多孔質構造によ
ってイオン伝導路が遮断されたり、添加物などでイオン
伝導経路が遮断され、イオン伝導が速やかに行われず、
得られる電流密度が小さくなって、いずれも電解液の介
在なくしてはエネルギー密度の高い二次電池とはなら
ず、実用性に欠けるという問題があった。In general, in an all solid state secondary battery, the performance of the battery can be improved by rapidly conducting ionic conduction in the solid electrolyte. Therefore, the solid electrolyte having a smaller number of defects that inhibit ionic conduction therein is better. It serves as an ion conductor to improve charge / discharge performance. However, in the above proposal, the ionic conduction path is interrupted by the porous structure of the solid electrolyte itself, or the ionic conduction path is interrupted by an additive or the like, and the ionic conduction is not performed promptly.
The resulting current density is low, and without any intervening electrolytic solution, a secondary battery having a high energy density cannot be obtained, and there is a problem that practicality is lacking.
【0008】[0008]
【発明の目的】このような課題を解決するために本発明
者等が鋭意検討した結果、大電流を取り出せない要因
は、固体電解質粒子間の界面の接触抵抗が高いことにあ
り、イオン伝導性を左右するこの界面でのイオン伝導を
速やかに行なわせることで固体電解質内における抵抗の
低減化を図ることが可能になることを知見した。The inventors of the present invention have conducted intensive studies in order to solve the above-mentioned problems. As a result, the reason why a large current cannot be taken out is that the contact resistance at the interface between the solid electrolyte particles is high and the ionic conductivity is high. It has been found that it is possible to reduce the resistance in the solid electrolyte by promptly conducting the ionic conduction at this interface which affects the resistance.
【0009】本発明は、このような知見に基づいてなさ
れたものであり、その目的は電池としての充放電のレー
ト特性や保存性などの諸特性が向上した固体電解質電池
を提供することにあり、特に二次電池としてサイクル特
性に優れたエネルギー密度の高い電解液を全く含まない
固体電解質電池を提供することにある。The present invention has been made based on such knowledge, and an object of the present invention is to provide a solid electrolyte battery having improved characteristics such as charge / discharge rate characteristics and storage stability as a battery. In particular, it is an object of the present invention to provide a solid electrolyte battery which is excellent in cycle characteristics and contains no high-energy-density electrolytic solution at all.
【0010】[0010]
【課題を解決するための手段】上記目的を達成するため
に、請求項1に係る固体電解質電池では、正極活物質と
負極活物質から成る一対の電極間に固体電解質を介在さ
せてなる固体電解質電池において、前記固体電解質と同
じ材料から成る無機酸化物が三次元ネットワークを構成
するように前記正極活物質あるいは負極活物質の粒子間
に介在させたことを特徴とする。According to a first aspect of the present invention, there is provided a solid electrolyte battery having a solid electrolyte interposed between a pair of electrodes comprising a positive electrode active material and a negative electrode active material. In the battery, an inorganic oxide made of the same material as the solid electrolyte is interposed between particles of the positive electrode active material or the negative electrode active material so as to form a three-dimensional network.
【0011】上記固体電解質電池では、前記正極活物質
あるいは負極活物質の粒子間に介在させた無機酸化物が
前記固体電解質に連続して存在することが望ましい。In the above solid electrolyte battery, it is preferable that the inorganic oxide interposed between the particles of the positive electrode active material or the negative electrode active material is continuously present in the solid electrolyte.
【0012】また、請求項3に係る固体電解質電池の製
造方法では、正極活物質と無機酸化物との混合物、無機
酸化物、および負極活物質と無機酸化物との混合物をそ
れぞれシート状に成形して積層した後、相対密度が80
%以上になるように焼成して、正極、固体電解質、およ
び負極を形成する。According to a third aspect of the present invention, in the method for manufacturing a solid electrolyte battery, a mixture of a positive electrode active material and an inorganic oxide, an inorganic oxide, and a mixture of a negative electrode active material and an inorganic oxide are each formed into a sheet. After lamination, the relative density is 80
% To form a positive electrode, a solid electrolyte, and a negative electrode.
【0013】[0013]
【作用】本発明の固体電解質電池によれば、電極内にお
いて固体電解質と同じ材料から成る無機酸化物が三次元
ネットワークを構成することから、電極内においては固
体電解質粒子同志の接触によって、その緻密なネットワ
ーク構造の構築が電極表面にまで形成可能になる。According to the solid electrolyte battery of the present invention, the inorganic oxide made of the same material as the solid electrolyte forms a three-dimensional network in the electrode. A network structure can be formed even on the electrode surface.
【0014】しかも、電極間に介在する同じ無機酸化物
からなる固体電解質とも接続された一体の構造体を形成
することができ、一対の電極の全体にわたって三次元ネ
ットワーク構造の構築が可能となるものである。In addition, an integral structure connected to the solid electrolyte made of the same inorganic oxide interposed between the electrodes can be formed, and a three-dimensional network structure can be constructed over the entire pair of electrodes. It is.
【0015】このように電極内部でイオン伝導が速やか
に行なわれる構造をとることで、電池から大電流の取り
出しが可能となるものである。また、イオン移動を妨げ
るような固体電解質粒子間の界面での反応がないこと
で、不可逆な反応が低減し、その充放電サイクル性能に
おいてはより性能向上につながるものである。By employing a structure in which ionic conduction is rapidly performed inside the electrode as described above, a large current can be extracted from the battery. In addition, since there is no reaction at the interface between the solid electrolyte particles that hinders ion transfer, irreversible reaction is reduced, and the charge / discharge cycle performance is further improved.
【0016】さらには、加熱加圧成形で緻密化ができ、
取り出せる体積当たりのエネルギー量が向上することで
高エネルギー密度化が可能となるものである。Further, densification can be performed by heat and pressure molding,
By increasing the amount of energy per volume that can be taken out, high energy density can be achieved.
【0017】[0017]
【発明の実施の形態】以下、本発明を図面に基づき詳細
に説明する。図1は、本発明の固体電解質電池をコイン
型電池に適用した一例を示す断面図である。図1におい
て、1は正極、2は負極、3は固体電解質、4は正極集
電体層、5は負極集電体層、6はスプリングばね、7は
正極缶、8は負極缶、9は絶縁パッキングである。固体
電解質3を挟持した一対の電極1、2の外表面に蒸着膜
から成る集電体層4、5を設けて主要部を構成し、スプ
リングスペーサ6で圧迫して電池ケース缶7、8と接触
を確保し、その外周を樹脂充填パッキング9で密封して
コイン型電池を形成している。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to the drawings. FIG. 1 is a sectional view showing an example in which the solid electrolyte battery of the present invention is applied to a coin-type battery. In FIG. 1, 1 is a positive electrode, 2 is a negative electrode, 3 is a solid electrolyte, 4 is a positive electrode current collector layer, 5 is a negative electrode current collector layer, 6 is a spring, 7 is a positive electrode can, 8 is a negative electrode can, 9 is Insulation packing. Current collector layers 4 and 5 made of a vapor-deposited film are provided on the outer surfaces of a pair of electrodes 1 and 2 sandwiching the solid electrolyte 3 to constitute a main part, and are pressed by spring spacers 6 to form battery case cans 7 and 8. Contact is ensured, and the outer periphery is sealed with a resin-filled packing 9 to form a coin-type battery.
【0018】本発明の電極1、2としては、電気化学的
な酸化還元反応でリチウムイオンを吸蔵および放出させ
ることが可能なマンガン(Mn)、コバルト(Co)、
ニッケル(Ni)、バナジウム(V)、ニオブ(Nb)
の少なくとも一種を含む金属酸化物などが用いられ、特
にリチウムイオンを供給および移動させることが可能な
例えばFe2 O3 、TiO2 、Nb2 O3 、V2 O5 、
WO3 などの金属酸化物、望ましくはマンガン(M
n)、チタン(Ti)、バナジウム(V)、ニオブ(N
b)の少なくとも一種を含む金属酸化物やLiMn2 O
4 などが好適である。この金属酸化物は例えば0.1〜
20μm程度の粒径を有する。As the electrodes 1 and 2 of the present invention, manganese (Mn), cobalt (Co), which can occlude and release lithium ions by an electrochemical oxidation-reduction reaction,
Nickel (Ni), vanadium (V), niobium (Nb)
Metal oxides containing at least one of the following are used. Particularly, for example, Fe 2 O 3 , TiO 2 , Nb 2 O 3 , V 2 O 5 , which can supply and move lithium ions,
Metal oxides such as WO 3 , preferably manganese (M
n), titanium (Ti), vanadium (V), niobium (N
b) metal oxide or LiMn 2 O containing at least one of
4 and the like are preferable. This metal oxide is, for example, 0.1 to
It has a particle size of about 20 μm.
【0019】正極1と負極2の電極材料を形成する活物
質は、選択した材料の充放電電位差によって決まる電池
作動電圧をどこにとるかによって決まるものであり、必
ずしも正極活物質1および負極活物質2は固定的なもの
ではなく、どの活物質の組み合わせを選択するかで、固
体電解質電池の作動電圧は変化する。The active materials forming the electrode materials of the positive electrode 1 and the negative electrode 2 are determined by where the battery operating voltage determined by the charge / discharge potential difference of the selected materials is obtained. Is not fixed, and the operating voltage of the solid electrolyte battery changes depending on which combination of active materials is selected.
【0020】従って、負極2の材料としては組み合わせ
方次第では正極1の材料としてあげた材料を選択しても
電池を構成することは可能である。Therefore, it is possible to construct a battery even if the materials listed as materials for the positive electrode 1 are selected as the material for the negative electrode 2 depending on the combination.
【0021】固体電解質3としてはリチウムイオンのイ
オン伝導性を有するものであれば特に限定されるもので
はないが、例えばLiAlTi(PO)やLiGeVO
などの結晶質固体電解質、30LiI−41Li2 O−
29P2 O5 や40Li2 O−35B2 O5 −25Li
NbO3 などの酸化物非晶質固体電解質などを用いるこ
とができる。なお、本発明の固体電解質電池では、移動
させるイオンの種類は特に限定されないが、とりわけリ
チウムイオンに対して有効であり、リチウム(Li)を
含む固体電解質3中のイオン伝導が電極活物質1、2か
らのイオン供給とバランスが取れていることで、速やか
に行われるものである。The solid electrolyte 3 is not particularly limited as long as it has ion conductivity of lithium ions. For example, LiAlTi (PO) or LiGeVO
Crystalline solid electrolyte such as, 30LiI-41Li 2 O-
29P 2 O 5 and 40Li 2 O-35B 2 O 5 -25Li
An oxide amorphous solid electrolyte such as NbO 3 can be used. In the solid electrolyte battery of the present invention, the type of ions to be transferred is not particularly limited, but is particularly effective for lithium ions, and the ionic conduction in the solid electrolyte 3 containing lithium (Li) is not limited to the electrode active material 1, This can be performed promptly because the ion supply from 2 is balanced.
【0022】図2に電極1、2の断面を模式的を示す。
対象となる固体電解質と同じ材料から成る無機酸化物1
0が活物質粒子11の間に、ポア12を介しながらも三
次元ネットワークを形成した状態で介在している。この
場合には、十分な緻密化を促進できないため、無機酸化
物による三次元ネットワークはその内部に界面13を構
成することから、ネットワークの構成が不十分となり、
イオン伝導の阻害要因となる。このため、より緻密体を
形成することで、イオン電導性の向上が図れ、レート特
性並びにサイクル充放電特性もさらに向上する。すなわ
ち、イオン伝導の阻害要因並びにサイクル性能劣化モー
ドの主原因となる固体電解質と活物質との界面や固体電
解質粒子間の界面でのトラップを引き起こさないために
も、緻密度は相対密度で82%以上、望ましくは93%
以上が好ましい。つまり、この三次元ネットワークは、
活物質の全ての粒子間で構成される必要はなく、金属酸
化物が存在しない活物質の粒子間が部分的に存在しても
構わない。FIG. 2 schematically shows a cross section of the electrodes 1 and 2.
Inorganic oxide 1 consisting of the same material as the target solid electrolyte
0 intervenes between the active material particles 11 while forming a three-dimensional network through the pores 12. In this case, since sufficient densification cannot be promoted, the three-dimensional network of the inorganic oxide forms the interface 13 therein, and thus the network configuration becomes insufficient.
It becomes a factor inhibiting ion conduction. Therefore, by forming a denser body, the ion conductivity can be improved, and the rate characteristics and the cycle charge / discharge characteristics can be further improved. That is, in order not to cause traps at the interface between the solid electrolyte and the active material and the interface between the solid electrolyte particles, which are the main causes of the ion conduction inhibition factor and the cycle performance deterioration mode, the density is 82% in relative density. Above, preferably 93%
The above is preferred. In other words, this three-dimensional network
It is not necessary to constitute between all the particles of the active material, and a part of the particles of the active material in which the metal oxide does not exist may be present.
【0023】[0023]
【実施例】(実施例1)先ず、正極活物質としてのLi
Mn2 O4 を85重量%と無機固体電解質としての30
LiI−41Li2 O−29P2 O5 を15重量%を十
分に混合した。この混合体に対して成形用バインダーと
してポリビニルアルコールを5重量%を外添加し、溶剤
としてトルエンを適量添加して成形用スラリーを調製し
た。このスラリーをドクターブレードで約50μmの厚
みのシート状に成形し、溶剤を蒸発させて所定寸法のシ
ートに切断した。このようにして作製したシート状電極
を450℃で20時間焼成した後、600℃で100k
gf/cm2 の加圧下で1時間焼成した。焼成体の厚み
は約30μmであった。EXAMPLES (Example 1) First, Li as a positive electrode active material was used.
85% by weight of Mn 2 O 4 and 30 as an inorganic solid electrolyte
LiI-41Li 2 O-29P 2 O 5 to 15 wt% and mixed well. To this mixture, 5% by weight of polyvinyl alcohol was externally added as a binder for molding, and an appropriate amount of toluene was added as a solvent to prepare a slurry for molding. This slurry was formed into a sheet having a thickness of about 50 μm using a doctor blade, and the solvent was evaporated to cut into a sheet having a predetermined size. After firing the sheet electrode thus manufactured at 450 ° C. for 20 hours, the sheet electrode was heated at 600 ° C. for 100 k.
Firing was performed for 1 hour under a pressure of gf / cm 2 . The thickness of the fired body was about 30 μm.
【0024】負極活物質としてLi4 Mn5 O12を用い
て、正極を作製したのと同様にして焼成体を作製した。
厚みは同じく30μmであったまた、固体電解質として
の30LiI−41Li2 O−29P2 O5 のみを正負
極と同様にバインダーを用いて成形用スラリーを調製し
た後、ドクターブレードで30μmの厚みに成形してシ
ートを作製した。作製したシートを切り出した後、電極
と同じく450℃で20時間焼成し、100kgf/c
m2 の圧力で加圧加熱成形した。出来上がりの厚みは約
15μmであった。これらいずれの焼成体も焼成した後
の分析においては、用いたバインダーの成分は残留して
いないことが確認できた。また、各焼成体の相対密度
は、正極93%、負極95%、固体電解質98%であっ
た。Using Li 4 Mn 5 O 12 as the negative electrode active material, a fired body was prepared in the same manner as the positive electrode.
The thickness was also 30 μm. Also, after preparing a molding slurry using only 30LiI-41Li 2 O-29P 2 O 5 as a solid electrolyte using a binder in the same manner as the positive and negative electrodes, the slurry was molded to a thickness of 30 μm with a doctor blade. Thus, a sheet was prepared. After cutting out the prepared sheet, it is baked at 450 ° C. for 20 hours in the same manner as the electrode, and 100 kgf / c
Press molding was performed at a pressure of m 2 . The finished thickness was about 15 μm. In the analysis after firing all of these fired bodies, it was confirmed that the components of the binder used did not remain. The relative density of each fired body was 93% for the positive electrode, 95% for the negative electrode, and 98% for the solid electrolyte.
【0025】次いで、正負両電極に対して、一方の面に
対してAuのアルゴンプラズマによるスパッタリングで
コンタクト電極を形成した。この3つの焼成体を150
℃で2時間乾燥した後、グローブボックス内でコイン型
電池を組み上げた。Au電極が外側になるように積層し
て電池の構成とした後、スプリングワッシャを挿入する
ことで、電極と電池缶との間の接触をとってコイン型電
池に組み上げた。Next, a contact electrode was formed on one of the positive and negative electrodes by sputtering with Au argon plasma. These three fired bodies are put in 150
After drying at 2 ° C. for 2 hours, a coin-type battery was assembled in a glove box. After laminating the Au electrode on the outside to form a battery, a spring washer was inserted to make contact between the electrode and the battery can to assemble the coin battery.
【0026】二次電池充放電装置で電池性能の測定を行
なった。充電条件として100μAの電流で評価用のコ
イン型電池に2.8Vまで充電を行い、電圧が2.8V
に到達した後、充電を停止して5分間保持し、その後
1.0Vの電圧まで100μAの放電電流で放電し、次
に2.8Vまで再充電して5分間保持する充放電サイク
ル試験を行い、一定サイクル毎に放電電気量を求めて二
次電池としての電池性能の評価を行った。The battery performance was measured with a secondary battery charging / discharging device. As a charging condition, the coin cell battery for evaluation was charged to 2.8 V with a current of 100 μA, and the voltage was 2.8 V.
After reaching, the charge was stopped and held for 5 minutes, then discharged to a voltage of 1.0 V with a discharge current of 100 μA, and then recharged to 2.8 V and held for 5 minutes. Then, the amount of discharge electricity was obtained for each fixed cycle, and the battery performance as a secondary battery was evaluated.
【0027】(比較例1)実施例1に示した方法によっ
て作製した各電極並びに固体電解質成形シートを加圧し
ない600℃の大気中で焼成して焼成体を作製した。こ
の焼成で得られた焼成体の相対密度は正極80%、負極
79%、固体電解質90%であった。(Comparative Example 1) Each electrode and the solid electrolyte molded sheet produced by the method shown in Example 1 were fired in the air at 600 ° C without pressurization to produce a fired body. The relative density of the fired body obtained by this firing was a positive electrode 80%, a negative electrode 79%, and a solid electrolyte 90%.
【0028】焼成体は、実施例1と同じ方法によって、
コイン型電池に組み上げて比較例とした。比較例の測定
も実施例1と同じ条件で行った。The fired body was prepared in the same manner as in Example 1.
A comparative example was set up in a coin-type battery. The measurement of the comparative example was also performed under the same conditions as in Example 1.
【0029】以上に示した実施例1並びに比較例1の両
サンプルの充放電測定結果を表1に示す。Table 1 shows the charging / discharging measurement results of both samples of Example 1 and Comparative Example 1 described above.
【0030】[0030]
【表1】 [Table 1]
【0031】実施例では充放電特性が確認できたのに対
し、比較例1では測定と同時に電圧が上限電圧に達して
しまい、切り替わった放電でもすぐに下限電圧に達して
しまうため、容量の測定はできなかった。In the example, the charge / discharge characteristics were confirmed. In contrast, in the comparative example 1, the voltage reached the upper limit voltage at the same time as the measurement, and immediately reached the lower limit voltage even in the switched discharge. Could not.
【0032】また、実施例1並びに比較例1で作製した
電極の焼成体を断面観察したところ、実施例1で作製し
た焼成体の断面においては、電極内部の粒子間において
金属酸化物の三次元ネットワークが形成され、十分な緻
密化が進んでいることが確認された。一方、比較例にお
いては図2に模式図で示したようなポア12とみられる
欠陥が多数確認でき、粒子間において固体電解質のネッ
トワークが未発達であることが確認された。Further, when the cross section of the fired body of the electrode manufactured in Example 1 and Comparative Example 1 was observed, in the cross section of the fired body manufactured in Example 1, the three-dimensional metal oxide was formed between the particles inside the electrode. It was confirmed that a network had been formed and that sufficient densification had progressed. On the other hand, in the comparative example, many defects such as the pores 12 shown in the schematic diagram of FIG. 2 were confirmed, and it was confirmed that the solid electrolyte network was not developed between the particles.
【0033】(実施例2)上記実施例1において加圧焼
成で作製したAuから成るコンタクト電極の形成前の各
焼成体電極を固体電解質シートで挟んで積層して電池構
成とした後に、実施例1と同様に650℃において10
0kgf/cm2 の圧力で15分間の焼成を行なって一
体とした。作製した一体構造の電池の相対密度を測定し
たところ、95%であることが確認された。(Example 2) In Example 1, after each fired body electrode before forming the contact electrode made of Au produced by pressure firing in Example 1 was sandwiched between solid electrolyte sheets to form a battery. 10 at 650 ° C as in 1
Firing was performed at a pressure of 0 kgf / cm 2 for 15 minutes to obtain an integrated body. When the relative density of the manufactured battery having an integral structure was measured, it was confirmed to be 95%.
【0034】(比較例2)実施例1において加圧焼成で
作製した各焼成体と固体電解質を実施例2と同様に積層
して電池構成とした後、平板セラミックスプレート上に
おいて加圧しないで大気中650℃で15分間の焼成を
行った。この焼成体の相対密度は78%であった。(Comparative Example 2) Each fired body produced by pressure firing in Example 1 and a solid electrolyte were laminated in the same manner as in Example 2 to form a battery. Firing was performed at 650 ° C. for 15 minutes. The relative density of this fired body was 78%.
【0035】これら実施例2、比較例2の各積層焼成体
の両面にスパッタリング法でAuから成るコンタクト電
極を形成し、実施例1と同様にコイン型電池に組み上げ
て充放電測定を行った。作製した電池の充放電特性の結
果を表2に示す。Contact electrodes made of Au were formed on both sides of each of the laminated fired bodies of Example 2 and Comparative Example 2 by a sputtering method, and assembled into a coin-type battery in the same manner as in Example 1 to perform charge / discharge measurement. Table 2 shows the results of the charge / discharge characteristics of the manufactured batteries.
【0036】[0036]
【表2】 [Table 2]
【0037】実施例2においては、初期容量が85 μA
hと比較例の倍以上であり、しかも初期容量比で80%
維持が60サイクル以上で可能であった。しかし比較例
では容量が低い上、サイクル特性の劣化が著しく18サ
イクルで80%以下の容量となり、電池の性能としての
違いは明らかであった。In the second embodiment, the initial capacity is 85 μA.
h and more than double the comparative example, and 80% of the initial capacity ratio
Maintenance was possible over 60 cycles. However, in the comparative example, the capacity was low and the deterioration of the cycle characteristics was remarkable, and the capacity was 80% or less in 18 cycles, and the difference in the performance of the battery was obvious.
【0038】この各電池の電極と固体電解質の接合界面
の観察を行なった。実施例2では電極内部のネットワー
クを持つ固体電解質と電極に挟まれた固体電解質の接合
部では、接合の界面は特に観察されず、良好な接合を形
成していることが確認された。一方、比較例2では電極
内部の固体電解質と電極に挟まれた固体電解質の接合部
において、部分的に実施例2と同様に良好な接合が形成
されていることが確認されたが、大多数の接合部におい
ては明らかに接合界面の形成が観察され、接合部におけ
る連続したネットワークが断絶していることが確認され
た。The junction interface between the electrode of each battery and the solid electrolyte was observed. In Example 2, at the junction between the solid electrolyte having a network inside the electrode and the solid electrolyte sandwiched between the electrodes, no particular interface of the junction was observed, and it was confirmed that a good junction was formed. On the other hand, in Comparative Example 2, it was confirmed that good bonding was partially formed as in Example 2 at the joint between the solid electrolyte inside the electrode and the solid electrolyte sandwiched between the electrodes. The formation of a joint interface was clearly observed at the joint of Example 1, and it was confirmed that a continuous network at the joint was broken.
【0039】実施例1および2、比較例1および2で示
したように、電極内部で無機酸化物が十分な三次元ネッ
トワークをとること、さらにはその無機酸化物が正電極
と負電極との間にある固体電解質とも接合されてネット
ワークが十分取れることで本発明の目的は達成されるも
のであり、実施例1および2、比較例1および2で示し
たように、固体電解質構造体は固体電解質と活物質の混
合体からなるシート状に成形された一対の電極間に、同
じくシート状に成形された固体電解質を挟んだ構成をと
る積層成形体を加圧加熱焼成することで固体電解質電池
が製造できる。As shown in Examples 1 and 2 and Comparative Examples 1 and 2, the inorganic oxide forms a sufficient three-dimensional network inside the electrode, and furthermore, the inorganic oxide forms a connection between the positive electrode and the negative electrode. The object of the present invention is achieved by bonding to the solid electrolyte in between to obtain a sufficient network, and as shown in Examples 1 and 2, and Comparative Examples 1 and 2, the solid electrolyte structure is a solid A solid electrolyte battery is obtained by pressurizing, heating and firing a laminated molded body having a configuration in which a solid electrolyte similarly molded into a sheet is sandwiched between a pair of electrodes molded into a sheet composed of a mixture of an electrolyte and an active material. Can be manufactured.
【0040】(実施例3)スラリーを調製して実施例1
と同様に正極、負極をドクターブレードでシート状に成
形し、溶剤を蒸発させて電極を作製した。実施例1と同
様にシートを成形して固体電解質を作製した。何れも4
50℃で20時間焼成した後、やはり実施例1と同じく
積層した後に650℃で加圧加熱焼成で緻密化を促進さ
せた。各サンプルの相対密度を成形圧力に対して示し
た。密度の測定にはアルキメデス法を用い、相対密度は
各原料の真比重を混合比に対して割り振ることで計算し
た。Example 3 Example 1 was prepared by preparing a slurry.
Similarly to the above, the positive electrode and the negative electrode were formed into a sheet shape using a doctor blade, and the solvent was evaporated to prepare an electrode. A sheet was formed in the same manner as in Example 1 to produce a solid electrolyte. All 4
After firing at 50 ° C. for 20 hours, the layers were laminated as in Example 1, and then densification was promoted by heating under pressure at 650 ° C. The relative density of each sample is shown relative to the molding pressure. The Archimedes method was used to measure the density, and the relative density was calculated by assigning the true specific gravity of each raw material to the mixture ratio.
【0041】実施例1と同様に電極を作製してコイン型
電池を構成して充放電測定を行なった。その結果を表3
に示す。Electrodes were produced in the same manner as in Example 1 to form a coin-type battery, and charge / discharge measurement was performed. Table 3 shows the results.
Shown in
【0042】[0042]
【表3】 [Table 3]
【0043】相対密度が80%未満のものについては単
位重量当たりの放電容量はある程度得られるものの、エ
ネルギー密度そのものの向上は図れず、とりわけサイク
ル特性において良好な結果は得られなかった。しかしな
がら、相対密度が80%以上の場合には、放電容量の絶
対値並びにサイクル性能がともに急速に向上することが
確認された。When the relative density was less than 80%, the discharge capacity per unit weight could be obtained to some extent, but the energy density itself could not be improved, and particularly good results could not be obtained in the cycle characteristics. However, it was confirmed that when the relative density was 80% or more, both the absolute value of the discharge capacity and the cycle performance were rapidly improved.
【0044】なお、発明の趣旨を逸脱しない範囲であれ
ば、加圧加熱焼成による温度ならびに圧力、加圧時間は
種々変更可能である。It should be noted that the temperature, pressure, and pressurizing time by pressurizing, heating and firing can be variously changed without departing from the spirit of the invention.
【0045】また、本発明は前記実施形態に限定される
ものではなく、角型、薄型の電池に適用した場合でも、
要旨を逸脱しない範囲であれば種々変更可能である。Further, the present invention is not limited to the above embodiment, and even when applied to a rectangular or thin battery,
Various changes can be made without departing from the scope.
【0046】[0046]
【発明の効果】以上のように、本発明に係る固体電解質
電池によれば、固体電解質と同じ材料から成る無機酸化
物が三次元ネットワークを構成するように正極活物質あ
るいは負極活物質の粒子間に介在させたことから、固体
電解質が電極活物質間並びに電極間において三次元のネ
ットワーク構造を持つ焼成体の一体構造をとることで、
電解質内における粒子間の接触界面を天元し、固体電解
質間におけるイオン伝導を速やかにするものである。ま
た、このイオン伝導経路としての三次元ネットワーク構
造は緻密度をあげることで、さらに伝導性の良好なイオ
ン電導性固体電解質として作用することが可能となり、
このことより電池内部でのイオン伝導の阻害要因として
の分極が低減され、電池自体の内部抵抗が小さくなり、
固体内部におけるイオン伝導が速やかに行われること
で、電池から取り出せる電流は大きなものが得られ、く
り返し充放電によるサイクル劣化の要因であるイオン伝
導のトラップを防止することが可能となるものであり、
その産業上の利用価値は極めて高いものである。As described above, according to the solid electrolyte battery of the present invention, the particles of the positive electrode active material or the negative electrode active material are formed so that the inorganic oxide composed of the same material as the solid electrolyte forms a three-dimensional network. Since the solid electrolyte has an integrated structure of a fired body having a three-dimensional network structure between the electrode active materials and between the electrodes,
The purpose is to balance the contact interface between particles in the electrolyte and to speed up ionic conduction between the solid electrolytes. In addition, by increasing the density of the three-dimensional network structure as the ion conduction path, it becomes possible to act as an ion-conductive solid electrolyte having better conductivity,
This reduces polarization as a factor inhibiting ion conduction inside the battery, lowering the internal resistance of the battery itself,
By rapidly conducting ion conduction inside the solid, a large current can be obtained from the battery, and it is possible to prevent trapping of ion conduction, which is a cause of cycle deterioration due to repeated charging and discharging,
Its industrial utility value is extremely high.
【図1】本発明の固体電解質電池をコイン型電池に適用
した一実施例を示す断面図である。FIG. 1 is a cross-sectional view showing one embodiment in which a solid electrolyte battery of the present invention is applied to a coin-type battery.
【図2】本発明の固体電解質電池における活物質粒子と
固体電解質の接触を示した断面図である。FIG. 2 is a cross-sectional view showing contact between active material particles and a solid electrolyte in the solid electrolyte battery of the present invention.
1‥‥‥正極、2‥‥‥負極、3‥‥‥固体電解質、4
‥‥‥正極集電体層、5‥‥‥負極集電体層、6‥‥‥
スプリングばね、7‥‥‥正極缶、8‥‥‥負極缶、9
‥‥‥絶縁パッキング、10‥‥‥三次元固体電解質構
造体、11‥‥‥活物質粒子、12‥‥‥ポア、13‥
‥‥固体電解質界面1 ‥‥‥ cathode, 2 ‥‥‥ anode, 3 ‥‥‥ solid electrolyte, 4
{Positive electrode current collector layer, 5} Negative electrode current collector layer, 6}
Spring spring, 7 mm positive can, 8 mm negative can, 9
{Insulating packing, 10} three-dimensional solid electrolyte structure, 11 {active material particles, 12} pore, 13}
‥‥ Solid electrolyte interface
───────────────────────────────────────────────────── フロントページの続き (72)発明者 馬込 伸二 京都府相楽郡精華町光台3丁目5番地 京 セラ株式会社中央研究所内 (72)発明者 大崎 誠 京都府相楽郡精華町光台3丁目5番地 京 セラ株式会社中央研究所内 (72)発明者 原 亨 京都府相楽郡精華町光台3丁目5番地 京 セラ株式会社中央研究所内 (72)発明者 樋口 永 京都府相楽郡精華町光台3丁目5番地 京 セラ株式会社中央研究所内 Fターム(参考) 5H003 AA01 AA02 AA03 AA04 BA01 BA03 BB12 BC05 BC06 BD05 5H029 AJ02 AJ03 AJ04 AJ05 AK02 AK03 AL02 AL03 AM12 BJ03 BJ12 CJ02 CJ06 CJ08 HJ08 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Shinji Magome 3-5 Koikadai, Seika-cho, Soraku-gun, Kyoto Prefecture Inside the Central Research Laboratory, Kyocera Corporation (72) Inventor Makoto Osaki 3-chome Koikadai, Soraku-gun, Kyoto Prefecture 5 Kyocera Corporation Central Research Laboratory (72) Inventor Tohru Hara 3-chome, Seika-cho, Soraku-gun, Kyoto Prefecture 5-5-2 Kyocera Corporation Central Research Laboratory (72) Inventor Ei Higuchi Seika-cho, Soraku-gun, Kyoto Prefecture 3-5-5 Kyocera Corporation Central Research Laboratory F-term (reference) 5H003 AA01 AA02 AA03 AA04 BA01 BA03 BB12 BC05 BC06 BD05 5H029 AJ02 AJ03 AJ04 AJ05 AK02 AK03 AL02 AL03 AM12 BJ03 BJ12 CJ02 CJ06 CJ08 HJ08
Claims (3)
電極間に固体電解質を介在させてなる固体電解質電池に
おいて、前記固体電解質と同じ材料から成る無機酸化物
が三次元ネットワークを構成するように前記正極活物質
あるいは負極活物質の粒子間に介在させたことを特徴と
する固体電解質電池。1. A solid electrolyte battery in which a solid electrolyte is interposed between a pair of electrodes composed of a positive electrode active material and a negative electrode active material, wherein an inorganic oxide composed of the same material as the solid electrolyte forms a three-dimensional network. Wherein a solid electrolyte battery is interposed between particles of the positive electrode active material or the negative electrode active material.
子間に介在させた無機酸化物が前記固体電解質に連続し
て存在することを特徴とする請求項1に記載の固体電解
質電池。2. The solid electrolyte battery according to claim 1, wherein the inorganic oxide interposed between the particles of the positive electrode active material or the negative electrode active material is continuously present in the solid electrolyte.
機酸化物、および負極活物質と無機酸化物との混合物を
それぞれシート状に成形して積層した後、相対密度が8
0%以上になるように焼成して、正極、固体電解質、お
よび負極を形成する固体電解質電池の製造方法。3. A sheet obtained by forming a mixture of the positive electrode active material and the inorganic oxide, the inorganic oxide, and the mixture of the negative electrode active material and the inorganic oxide into a sheet shape and laminating the same, and then having a relative density of 8%.
A method for producing a solid electrolyte battery in which a positive electrode, a solid electrolyte, and a negative electrode are formed by firing to 0% or more.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11120381A JP2000311710A (en) | 1999-04-27 | 1999-04-27 | Solid electrolyte battery and method of manufacturing the same |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1826860A1 (en) * | 2006-02-24 | 2007-08-29 | Ngk Insulators, Ltd. | All-solid-state battery |
| WO2008059987A1 (en) | 2006-11-14 | 2008-05-22 | Ngk Insulators, Ltd. | Solid electrolyte structure for all-solid-state battery, all-solid-state battery, and their production methods |
| US7510800B2 (en) | 2006-02-24 | 2009-03-31 | Ngk Insulators, Ltd. | All-solid-state battery |
| EP2058881A1 (en) | 2007-11-12 | 2009-05-13 | Kyushu University | All-solid-state cell |
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