JP2017182949A - Method for manufacturing positive electrode substance material for all-solid battery, and positive electrode active substance material for all-solid battery - Google Patents

Method for manufacturing positive electrode substance material for all-solid battery, and positive electrode active substance material for all-solid battery Download PDF

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JP2017182949A
JP2017182949A JP2016064930A JP2016064930A JP2017182949A JP 2017182949 A JP2017182949 A JP 2017182949A JP 2016064930 A JP2016064930 A JP 2016064930A JP 2016064930 A JP2016064930 A JP 2016064930A JP 2017182949 A JP2017182949 A JP 2017182949A
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羊一郎 河野
Yoichiro Kono
羊一郎 河野
藤井 信三
Shinzo Fujii
信三 藤井
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Abstract

PROBLEM TO BE SOLVED: To use a compound including, as a transition metal M, one of Co and Ni, or both of them, and expressed by LiMPOas a positive electrode active material of an all-solid battery, which is manufactured by a green sheet method.SOLUTION: A method for manufacturing a positive electrode active substance material for an all-solid battery comprises: a mixing step (s1, s2) for weighing and mixing a raw material of a positive electrode active substance consisting of a compound expressed by the chemical formula, LiMPOwhere M includes one of Co and Ni or both of them; a primary baking step (s3) for preliminarily baking a mixture obtained by the mixing step in an ambient atmosphere; a secondary baking step (s5) for baking powder of the mixture after the primary baking step at a temperature higher than that in the primary baking step in an ambient atmosphere; and a pulverizing step (s6) for pulverizing a sintered compact obtained by the secondary baking step. In the secondary baking step, the powder is baked at a temperature of 650-680°C for 20 to 30 hours.SELECTED DRAWING: Figure 1

Description

本発明は全固体電池に用いられる正極活物質材料の製造方法およびその製造方法で製造された正極活物質材料に関する。   The present invention relates to a method for producing a positive electrode active material used for an all-solid battery and a positive electrode active material produced by the method.

電気自動車、携帯情報端末、定置型蓄電設備などでは、高容量の二次電池が利用され、現在の二次電池の主流はリチウム二次電池である。リチウム二次電池用の正極活物質としては、LiCoO、LiMnなどが知られているが、これらの正極活物質は一つの遷移金属に対して一つのLiしか関与しないため、より高容量のリチウム二次電池を達成するためには、一つの遷移金属に対して複数のLiが関与する、所謂「多電子反応」を示す正極活物質を含む正極層材料を開発することが必要となる。そして多電子反応を示す正極活物質では、複数のLiがレドックス反応に寄与することから、より高電位で動作し、高容量とともに高いエネルギー密度も得られる。ところが一般に普及しているリチウム二次電池は、電解質に可燃性の有機電解液を用いているため、液漏れ、短絡、過充電などに対する安全対策が他の電池よりも厳しく求められている。そして多電子反応を示す正極活物質は、高電位で動作することから有機電解液を用いた従来のリチウム二次電池に用いることが難しい。 High capacity secondary batteries are used in electric vehicles, portable information terminals, stationary power storage facilities, etc., and the current mainstream of secondary batteries is lithium secondary batteries. As positive electrode active materials for lithium secondary batteries, LiCoO 2 , LiMn 2 O 4 and the like are known. However, since these positive electrode active materials involve only one Li for one transition metal, they are more expensive. In order to achieve a lithium secondary battery having a capacity, it is necessary to develop a positive electrode layer material including a positive electrode active material exhibiting a so-called “multi-electron reaction” in which a plurality of Lis are involved with one transition metal. Become. And in the positive electrode active material which shows a multi-electron reaction, since several Li contributes to a redox reaction, it operate | moves at a higher potential and high energy density is also obtained with high capacity | capacitance. However, since lithium secondary batteries that are widely used use a flammable organic electrolyte as an electrolyte, safety measures against leakage, short circuit, overcharge, and the like are required more strictly than other batteries. And since the positive electrode active material which shows a multi-electron reaction operate | moves with a high electric potential, it is difficult to use it for the conventional lithium secondary battery using an organic electrolyte solution.

そこで近年、電解質に酸化物系や硫化物系の固体電解質を用いた全固体電池に関する研究開発が盛んに行われている。固体電解質は、固体中でイオン伝導が可能なイオン伝導体を主体として構成される材料であり、従来のリチウム二次電池のように可燃性の有機電解液に起因する各種問題が原理的に発生しない。そして全固体電池は層状の正極(正極層)と層状の負極(負極層)との間に層状の固体電解質(電解質層)が狭持されてなる一体的な焼結体(以下、積層電極体とも言う)に集電体を形成した構造を有している。   In recent years, therefore, research and development have been actively conducted on all-solid-state batteries using oxide-based or sulfide-based solid electrolytes as electrolytes. Solid electrolytes are mainly composed of ionic conductors that can conduct ions in solids, and in principle, various problems caused by flammable organic electrolytes occur like conventional lithium secondary batteries. do not do. An all-solid battery is an integrated sintered body (hereinafter referred to as a laminated electrode body) in which a layered solid electrolyte (electrolyte layer) is sandwiched between a layered positive electrode (positive electrode layer) and a layered negative electrode (negative electrode layer). Also has a structure in which a current collector is formed.

上述した「多電子反応」が期待できる全固体電池用の正極活物質としては、例えば、LiMPの化学式(Mは遷移金属)で表される化合物があり、以下の非特許文献1や2にはMをFeとしたLiFeP(ピロリン酸鉄リチウム)の特性などについて記載されている。また上記LiMPにおいて、遷移金属MとしてCoとNiの一方あるいは双方を含む化合物は、化学式の上では一つのMに対して2個のLiがレドックス反応に寄与することが可能であり、極めて高い容量とエネルギー密度を有した正極活物質として期待されている。 Examples of the positive electrode active material for an all solid state battery that can be expected to have the above-mentioned “multi-electron reaction” include, for example, a compound represented by the chemical formula of Li 2 MP 2 O 7 (M is a transition metal). 1 and 2 describe characteristics of Li 2 FeP 2 O 7 (lithium iron pyrophosphate) in which M is Fe. In the above Li 2 MP 2 O 7 , in the compound containing one or both of Co and Ni as the transition metal M, two Li can contribute to the redox reaction for one M on the chemical formula. It is expected as a positive electrode active material having extremely high capacity and energy density.

なお全固体電池の本体となる上記積層電極体の製造方法としては、周知のグリーンシートを用いた方法がある。概略的には、正極活物質と固体電解質を含むスラリー状の正極層材料、負極活物質と固体電解質を含むスラリー状の負極層材料、および固体電解質を含むスラリー状の固体電解質層材料をそれぞれシート状(グリーンシート)に成形するとともに、固体電解質層材料のグリーンシートを正極層材料と負極層材料のグリーンシートで挟持した積層体を焼成して焼結体にすることで作製される。なお各層のグリーンシートを作製する方法としては、周知のドクターブレード法がある。ドクターブレード法では、無機酸化物などのセラミックス粉体にバインダ(ポリビニルアルコール(PVA)、ポリビニルブチラール(PVB)、ポリフッ化ビニリレン(PVDF)、アクリル、エチルメチルセルロースなど)および溶剤(無水アルコールなど)を混合して得たスラリーを塗布工程あるいは印刷工程により薄板状に成形してグリーンシートを作製する。そしてスラリーに含ませるセラミック粉体として正極活物質、固体電解質、および負極活物質のそれぞれの粉体を用いる。   In addition, as a manufacturing method of the said laminated electrode body used as the main body of an all-solid-state battery, there exists the method using a known green sheet. Schematically, a slurry-like positive electrode layer material containing a positive electrode active material and a solid electrolyte, a slurry-like negative electrode layer material containing a negative electrode active material and a solid electrolyte, and a slurry-like solid electrolyte layer material containing a solid electrolyte are each sheeted. It is produced by forming a green body (green sheet) and firing a laminated body in which a solid electrolyte layer material green sheet is sandwiched between a positive electrode layer material and a negative electrode layer material green sheet to form a sintered body. In addition, as a method of producing the green sheet of each layer, there is a known doctor blade method. In the doctor blade method, a binder (polyvinyl alcohol (PVA), polyvinyl butyral (PVB), polyvinylidene fluoride (PVDF), acrylic, ethylmethylcellulose, etc.) and a solvent (anhydrous alcohol, etc.) are mixed with ceramic powder such as inorganic oxide. The slurry obtained in this manner is formed into a thin plate by a coating process or a printing process to produce a green sheet. Then, each powder of the positive electrode active material, the solid electrolyte, and the negative electrode active material is used as the ceramic powder to be included in the slurry.

Shin-ichi Nishimura,Megumi Nakamura,Ryuichi Natsui,and AtsuoYamada、「New Lithium Iron Pyrophosphate as 3.5V Class Cathode Material for Lithium Ion Battery」、J.Am.Chem.Soc.、2010,132(39),pp13596-13597Shin-ichi Nishimura, Megumi Nakamura, Ryuichi Natsui, and Atsuo Yamada, `` New Lithium Iron Pyrophosphate as 3.5V Class Cathode Material for Lithium Ion Battery '', J. Am. Chem. Soc., 2010, 132 (39), pp 13596-13597 Hui Zhou,Shailesh Upreti,Natasha A.Chernova,Geoffroy Hautier,Gerbrand Ceder,and M. Stanley Whittingham、「Iron and Manganese Pyrophosphates as Cathodes for Lithium-Ion Batteries」、Chem. Mater.、2011,23(2),pp293-300Hui Zhou, Shailesh Upreti, Natasha A. Chernova, Geoffroy Hautier, Gerbrand Ceder, and M. Stanley Whittingham, "Iron and Manganese Pyrophosphates as Cathodes for Lithium-Ion Batteries", Chem. Mater., 2011, 23 (2), pp293 -300

上述したように全固体電池の製造方法の主体は、グリーシートからなる積層体を焼結させて積層電極体を作製することにあるが、上記化学式LiMPで表され、遷移金属MとしてCoとNiの一方あるいは双方を含む化合物は、理論上では高容量、高エネルギー密度が得られる正極活物質として有望であるものの、現状では、その化合物をグリーンシート法によって製造される全固体電池の正極活物質として実際に使用するための検討がほとんどなされていない。すなわちグリーンシート法によって全固体電池を製造する過程で、正極活物質からなる焼結体を粉砕してセラミック粉体の状態にするための検討や、そのセラミック粉体からなる正極活物質(以下、正極活物質材料とも言う)と粉体状の固体電解質とを含んだグリーンを焼成によって積層電極体における正極層として確実に焼結させるための検討などがなされていない。 As described above, the main method of manufacturing the all-solid-state battery is to sinter a laminated body made of a green sheet to produce a laminated electrode body, which is represented by the above chemical formula Li 2 MP 2 O 7 and is a transition metal. A compound containing one or both of Co and Ni as M is theoretically promising as a positive electrode active material capable of obtaining a high capacity and high energy density, but at present, the compound is an all solid produced by a green sheet method. There has been little study for practical use as a positive electrode active material for batteries. That is, in the process of producing an all-solid-state battery by the green sheet method, a study for pulverizing a sintered body made of a positive electrode active material into a ceramic powder state, a positive electrode active material made of the ceramic powder (hereinafter, No study has been made to reliably sinter green containing a positive electrode active material) and a powdered solid electrolyte as a positive electrode layer in a laminated electrode body by firing.

そこで本発明は、遷移金属MとしてCoとNiの一方あるいは双方を含む含んだLiMPで表される化合物をグリーンシート法によって製造される全固体電池の正極活物質として実際に使用できるようにするための全固体電池用正極活物質材料の製造方法を提供することを目的としている。またその製造方法によって作製された正極活物質材料を提供することも目的としている。 Therefore, the present invention actually uses a compound represented by Li 2 MP 2 O 7 containing one or both of Co and Ni as the transition metal M as a positive electrode active material of an all-solid battery manufactured by the green sheet method. It aims at providing the manufacturing method of the positive electrode active material material for all-solid-state batteries for enabling it. Another object of the present invention is to provide a positive electrode active material produced by the manufacturing method.

上記目的を達成するための本発明は、全固体電池用の正極活物質材料の製造方法であって、
化学式LiMPで表されるとともに、当該化学式中のMがCoとNiの一方あるいは双方を含む化合物からなる正極活物質の原材料を秤量して混合する混合ステップと、
前記混合ステップにより得た混合物を大気雰囲気中で仮焼成する一次焼成ステップと、
当該一次焼成ステップ後の前記混合物の粉体を当該一次焼成ステップよりも高い温度で大気雰囲気中で焼結させる二次焼成ステップと、
前記二次焼成ステップにより得た焼結体を粉砕する粉砕ステップと、
を含み、
前記二次焼成ステップでは、650℃以上680℃以下の温度で20時間以上30時間以下の時間で焼成すること、
を特徴とする全固体電池用正極活物質材料の製造方法としている。
The present invention for achieving the above object is a method for producing a positive electrode active material for an all solid state battery,
A mixing step of weighing and mixing the raw material of the positive electrode active material represented by the chemical formula Li 2 MP 2 O 7 , wherein M in the chemical formula is a compound containing one or both of Co and Ni;
A primary firing step in which the mixture obtained by the mixing step is temporarily fired in an air atmosphere;
A secondary firing step of sintering the powder of the mixture after the primary firing step in an air atmosphere at a temperature higher than the primary firing step;
A pulverizing step of pulverizing the sintered body obtained by the secondary firing step;
Including
In the secondary firing step, firing at a temperature of 650 ° C. to 680 ° C. for a time of 20 hours to 30 hours,
This is a method for producing a positive electrode active material for an all solid state battery.

また前記粉砕ステップ、あるいは当該粉砕ステップによって得た粉砕物を解砕するステップを実行することで、1μm以上7μm以下の平均粒子径を有する正極活物質材料を得ることを特徴とする全固体電池用正極活物質材料の製造方法とすれば好ましい。さらに本発明は上記製造方法によって製造された全固体電池用正極活物質材料にも及んでおり、当該全固体電池用正極活物質材料は、LiMPで表されるとともに、当該化学式中のMがCoとNiの一方あるいは双方を含む化合物を含み、異相を含まない結晶構造を有する前記化合物の焼結体が粉体状に粉砕されてなることを特徴としている。 Further, a positive electrode active material having an average particle diameter of 1 μm or more and 7 μm or less is obtained by executing the pulverization step or the step of pulverizing the pulverized material obtained by the pulverization step. A method for producing a positive electrode active material is preferable. Furthermore, the present invention extends to a positive electrode active material for all solid state batteries produced by the above production method. The positive electrode active material for all solid state batteries is represented by Li 2 MP 2 O 7 and has the chemical formula It is characterized in that a sintered body of the compound having a crystal structure in which M in the inside contains a compound containing one or both of Co and Ni and does not contain a different phase is pulverized into a powder form.

本発明の全固体電池用正極活物質の製造方法によれば、LiMPで表される化合物(MはCoとNiの一方あるいは双方を含む遷移金属)を全固体電池の正極活物質として実用化させることができる。そして当該製造方法によって製造される正極活物質材料は、多電子反応を示す正極活物質を含んだセラミック粉体であり、正極活物質材料を含む正極層を備えた全固体電池をグリーンシート法によって作製することができる。そのため大容量でエネルギー密度が高い全固体電池を安価に提供することができる。 According to the method for producing a positive electrode active material for an all solid state battery of the present invention, a compound represented by Li 2 MP 2 O 7 (M is a transition metal containing one or both of Co and Ni) is used as the positive electrode active material of the all solid state battery. It can be put into practical use as a substance. The positive electrode active material produced by the production method is a ceramic powder containing a positive electrode active material exhibiting a multi-electron reaction, and an all solid state battery including a positive electrode layer containing a positive electrode active material is obtained by a green sheet method. Can be produced. Therefore, an all-solid battery having a large capacity and a high energy density can be provided at low cost.

本発明の実施例に係る全固体電池用正極活物質材料の製造方法の流れを示す図である。It is a figure which shows the flow of the manufacturing method of the positive electrode active material material for all-solid-state batteries which concerns on the Example of this invention. 上記正極活物質材料の温度と熱収縮率との関係を示す図である。It is a figure which shows the relationship between the temperature of the said positive electrode active material material, and a thermal contraction rate.

===本発明に想到する過程===
周知のごとく、焼結体は多結晶材料であり、全固体電池の正極層や負極層(以下、総称して電極層とも言う)ではセラミック粉体の状態にある正極活物質材料や負極活物質材料(以下、総称して電極活物質材料とも言う)では、粉体を構成する個々の粒子が結晶化している。そして結晶化した際には個々の粒子が同じ結晶相であることが必要である。すなわち異相が混在する電極活物質のグリーンシートと固体電解質層のグリーンシートから構成される積層体を焼成して積層電極体として焼結させると、その積層電極体の電極層内には異相界面が存在することになる。そして異相界面では歪みや欠陥が発生し易く、焼結性が悪化する。そこで本発明者は、上述したLiMPで表される化合物(Mは少なくともCoとNiの一方を含む)を全固体電池の正極活物質として使用するために、グリーンシートに含ませるセラミック粉体の状態にある正極活物質材料の個々の粒子を同相にするための検討を行った。またその正極活物質材料を用いた全固体電池の容量をより高めるための検討も行った。そして本発明はこれらの検討事項に基づいて鋭意研究を重ねた結果なされたものである。
=== The process of conceiving the present invention ===
As is well known, the sintered body is a polycrystalline material, and the positive electrode active material and the negative electrode active material in the state of ceramic powder in the positive electrode layer and the negative electrode layer (hereinafter also collectively referred to as electrode layer) of the all-solid-state battery. In materials (hereinafter collectively referred to as electrode active material), individual particles constituting the powder are crystallized. When crystallized, it is necessary that the individual particles have the same crystal phase. That is, when a laminate composed of a green sheet of an electrode active material in which different phases are mixed and a green sheet of a solid electrolyte layer is fired and sintered as a laminated electrode body, there is a heterophase interface in the electrode layer of the laminated electrode body. Will exist. And distortion and a defect are easy to generate | occur | produce in a heterophase interface, and sintering property deteriorates. Therefore, the present inventor includes the above-described compound represented by Li 2 MP 2 O 7 (M includes at least one of Co and Ni) in the green sheet in order to use it as the positive electrode active material of the all-solid battery. A study was conducted to make individual particles of the positive electrode active material in a ceramic powder state in phase. In addition, studies were also conducted to further increase the capacity of the all-solid-state battery using the positive electrode active material. And this invention is made | formed as a result of repeating earnest research based on these examination matters.

===正極活物質材料の製造方法===
本発明の実施例に係る全固体電池用正極活物質材料の製造方法として、ピロリン酸コバルトリチウム(LiCoP、以下LCPOとも言う)を正極活物質とした正極活物質材料の製造手順を挙げる。図1に当該製造手順の流れを示した。まずLCPOの原料として(NH)HPO、LiCO、CoC・2HOを使用し、これらを化学量論比で秤量し(s1)、その原料を磁性乳鉢で混合した(s2)。そしてこのこれら原料の混合物をアルミナルツボに入れ、大気雰囲中、所定の温度で2時間加熱して仮焼き(以下、一次焼成とも言う)を行った(s3)。つぎに一次焼成後の上記混合物をメノウ乳鉢で粉砕して仮焼き粉体とし(s4)、その仮焼き粉体をアルミナルツボに入れて大気雰囲気中で本焼成(以下、二次焼成とも言う)して焼結体を得た(s5)。そしてその焼結体をメノウ乳鉢で粉砕して得たLCPOからなるセラミック粉体を正極活物質材料とする(s6)。
=== Method for Producing Positive Electrode Active Material ===
As a method for producing a positive electrode active material for an all solid state battery according to an embodiment of the present invention, a procedure for producing a positive electrode active material using lithium cobalt pyrophosphate (Li 2 CoP 2 O 7 , hereinafter also referred to as LCPO) as a positive electrode active material Give up. FIG. 1 shows the flow of the manufacturing procedure. First, (NH 4 ) 2 HPO 4 , Li 2 CO 3 , CoC 2 O 4 .2H 2 O are used as raw materials for LCPO, these are weighed in a stoichiometric ratio (s1), and the raw materials are mixed in a magnetic mortar. (S2). The mixture of these raw materials was placed in an alumina crucible, and pre-baked (hereinafter also referred to as primary firing) by heating at a predetermined temperature for 2 hours in the atmosphere (s3). Next, the mixture after primary firing is pulverized in an agate mortar to obtain a calcined powder (s4), and the calcined powder is placed in an alumina crucible and subjected to main firing in an air atmosphere (hereinafter also referred to as secondary firing). Thus, a sintered body was obtained (s5). And the ceramic powder which consists of LCPO obtained by grind | pulverizing the sintered compact with an agate mortar is made into a positive electrode active material material (s6).

このように上記の正極活物質材料の製造手順は、原料が異なるだけで他の正極活物質材料とほぼ同じである。しかし本実施例の製造方法では、二次焼成工程における温度と時間を最適化することで、作製された正極活物質材料中の粒子が全て同じ結晶相となるように制御している。しかも製造コストに鑑み、二次焼成を窒素雰囲気などではなく、大気雰囲気中で行うこととしている。すなわち二次焼成に際して焼成炉内を排気したり、炉内に不活性ガスを導入したりする必要がない。あるいは排気や不活性ガスの導入に必要な付帯装置がない安価な焼成炉を使用することが可能となる。なお上記製造手順における一次焼成工程(s3)は、周知のごとく、二次焼成工程(s5)よりも低い温度で原料を焼成することで、原料に含まれる炭酸や硝酸を離脱させて、原料を酸化させることである。すなわち一次焼成は大気雰囲気中であることが前提となる。したがって本実施例の製造方法によれば、一次焼成と二次焼成の双方を大気雰囲気中で行うことができる。   Thus, the manufacturing procedure of the positive electrode active material is substantially the same as that of other positive electrode active materials except that the raw materials are different. However, in the manufacturing method of this example, the temperature and time in the secondary firing step are optimized to control all the particles in the produced positive electrode active material material to have the same crystal phase. Moreover, in view of manufacturing costs, the secondary firing is performed in an air atmosphere instead of a nitrogen atmosphere or the like. That is, there is no need to exhaust the firing furnace or introduce an inert gas into the furnace during the secondary firing. Alternatively, it is possible to use an inexpensive firing furnace that does not have an incidental device necessary for introducing exhaust gas or inert gas. As is well known, the primary firing step (s3) in the above production procedure is performed by firing the raw material at a temperature lower than that of the secondary firing step (s5), thereby removing carbonic acid and nitric acid contained in the raw material, It is to oxidize. That is, the primary firing is premised on the atmosphere. Therefore, according to the manufacturing method of the present embodiment, both primary firing and secondary firing can be performed in an air atmosphere.

<二次焼成条件の最適化>
上述したように、本実施例の製造方法では、大気雰囲気中で二次焼成工程を行うこととし、その二次焼成工程における温度と時間を最適化することで正極活物質材料中の粒子が全て同じ結晶相となるように制御している。そこでこの二次焼成工程における条件(温度、時間)を最適化するために、図1に示した製造手順において、温度と時間を変えた様々な条件で二次焼成工程を行った。そしてその二次焼成後の焼結体に対してX線回折法を用いた結晶構造解析を行った。
<Optimization of secondary firing conditions>
As described above, in the manufacturing method of the present embodiment, the secondary firing step is performed in the air atmosphere, and all the particles in the positive electrode active material are obtained by optimizing the temperature and time in the secondary firing step. It is controlled so as to have the same crystal phase. Therefore, in order to optimize the conditions (temperature, time) in the secondary firing step, the secondary firing step was performed under various conditions in which the temperature and time were changed in the manufacturing procedure shown in FIG. And the crystal structure analysis which used the X ray diffraction method was performed with respect to the sintered compact after the secondary baking.

以下の表1に二次焼成工程の条件と当該結晶構造解析の結果との関係を示した。   Table 1 below shows the relationship between the conditions of the secondary firing step and the results of the crystal structure analysis.

Figure 2017182949
表1に示した結果から、650℃以上680℃以下の温度で20時間以上30時間以下の時間で焼成することで結晶構造に異相がない焼結体が得られることがわかった。したがって本発明の実施例では、この二次焼成条件によって得られた焼結体を粉砕したものを正極活物質材料とすることになる。なお650℃未満の温度でも焼成時間を30時間よりも長くすることで同相の結晶構造が得られる可能性もあるが、闇雲に焼成時間を長くしても製造コストを増大させるだけである。もちろん焼成時間が長ければ焼成後に炉内を冷却させる時間も長くなり製造高ストがさらに嵩むことになる。そこで本発明の実施例では、30時間以下の時間で二次焼成した際に異相がない結晶構造が得られることを条件として規定した。
Figure 2017182949
From the results shown in Table 1, it was found that a sintered body having no different phase in the crystal structure can be obtained by firing at a temperature of 650 ° C. to 680 ° C. for 20 hours to 30 hours. Therefore, in the Example of this invention, what grind | pulverized the sintered compact obtained by this secondary baking conditions will be used as a positive electrode active material material. Note that even if the firing time is longer than 30 hours even at a temperature lower than 650 ° C., a crystal structure of the same phase may be obtained, but even if the firing time is increased in the dark clouds, only the production cost is increased. Of course, if the firing time is long, the time for cooling the inside of the furnace after firing becomes long, and the manufacturing height is further increased. Therefore, in the examples of the present invention, it is defined as a condition that a crystal structure having no heterogeneous phase can be obtained when the secondary firing is performed for 30 hours or less.

===正極活物質材料の収縮率について===
本発明の実施例に係る製造方法で作製された正極活物質材料を用いて全固体電池を製造するためには、この正極活物質材料と粉体状の固体電解質とを含むスラリー状の正極層材料を用いてグリーンシートにすることになる。すなわち全固体電池における正極層内には正極活物質の他に電池容量に寄与しない固体電解質を含ませる必要がある。したがってより高容量の全固体電池を得るためには、正極層材料にイオン導電性が確保できる程度の固体電解質と、より多くの正極活物質とを含ませる必要がある。しかし従来の全固体電池では、正極層材料中に正極活物質材料と固体電解質とは質量比でほぼ同じ割合だけ含まれており、バインダや溶剤などを含めれば正極層材料内の正極活物質材料は50wt%未満である。
=== About Shrinkage Ratio of Positive Electrode Active Material Material ===
In order to produce an all-solid battery using the cathode active material produced by the production method according to the embodiment of the present invention, a slurry-like cathode layer containing the cathode active material and a powdered solid electrolyte is used. A green sheet is made using the material. That is, the positive electrode layer in the all-solid battery needs to contain a solid electrolyte that does not contribute to the battery capacity in addition to the positive electrode active material. Therefore, in order to obtain a higher-capacity all-solid battery, the positive electrode layer material needs to contain a solid electrolyte that can ensure ionic conductivity and a larger amount of the positive electrode active material. However, in the conventional all solid state battery, the positive electrode active material and the solid electrolyte are contained in the positive electrode layer material in almost the same ratio by mass ratio. If a binder, a solvent, etc. are included, the positive electrode active material in the positive electrode layer material Is less than 50 wt%.

そこで本発明者は、LCPOからなる粉体状の電極活物質材料を得るための最適な二次焼成条件を検討するのに並行して、より多くの正極活物質材料を正極層材料中に含ませることについても検討し、その検討過程でLCPOからなる粉体状の電極活物質材料は、スラリー状の正極層材料が正極層として焼結する際に収縮し、その収縮率が電極活物質材料の粒子径に応じて変化することに着目した。すなわち上記製造工程において、粉砕工程後の正極物質よりも大きな収縮率が得られれば、その収縮を見込んでより多くの正極活物質材料を正極層材料中に含ませることができると考えた。そして平均粒子径が異なる電極活物質材料を作製するとともに、焼結させた際の熱収縮率の差を調べた。平均粒子径が異なる電極活物質材料については、上述した製造工程によって製造した平均粒子径7μmの電極活物質材料をボールミルを用いてアルコール媒体中で所定時間解砕することで平均粒子径が1μm、2μm、3μm、5μmに調整された電極活物質材料を得た。したがって、解砕前の平均粒子径7μmの電極活物質材料と併せて、平均粒子径が異なる5種類の電極活物質材料を得た。   Accordingly, the present inventor included more positive electrode active material in the positive electrode layer material in parallel with studying the optimum secondary firing conditions for obtaining a powdered electrode active material made of LCPO. In the examination process, the powdered electrode active material made of LCPO shrinks when the slurry-like positive electrode layer material is sintered as the positive electrode layer, and the shrinkage rate is the electrode active material. It was noticed that it changed according to the particle diameter of the particles. That is, in the above manufacturing process, if a contraction rate larger than that of the positive electrode material after the pulverization process is obtained, it was considered that more positive electrode active material can be included in the positive electrode layer material in anticipation of the contraction. Then, electrode active material materials having different average particle diameters were prepared, and the difference in heat shrinkage ratio when sintered was examined. For electrode active material materials having different average particle diameters, an average particle diameter of 1 μm is obtained by crushing an electrode active material material having an average particle diameter of 7 μm manufactured by the above-described manufacturing process in an alcohol medium using a ball mill for a predetermined time. Electrode active material materials adjusted to 2 μm, 3 μm, and 5 μm were obtained. Therefore, together with the electrode active material having an average particle diameter of 7 μm before crushing, five types of electrode active material having different average particle diameters were obtained.

以下の表2に解砕時間と電極活物質材料の平均粒子径D50との関係を示した。 It shows the relationship between the average particle diameter D 50 between disintegration and the electrode active material in Table 2 below.

Figure 2017182949
表2に示したように、解砕時間が長いほど平均粒子径D50が小さくなる。そして12時間の解砕時間で平均粒子径1μmの電極活物質が得られた。もちろん、さらに長い時間を掛けて解砕すれば平均粒子径が1μm未満の微粉末からなる電極活物質材料も得られる。しかし解砕に長大な時間を掛ければ製造コストが増大する。また微粉末は僅かな気流によって容易に飛沫するので、取り扱いが難しいという問題もある。
Figure 2017182949
As shown in Table 2, average particle diameter D 50 the longer the inter-disintegration becomes smaller. And the electrode active material with an average particle diameter of 1 micrometer was obtained by the crushing time of 12 hours. Of course, an electrode active material made of fine powder having an average particle diameter of less than 1 μm can also be obtained by crushing for a longer time. However, if a long time is taken for crushing, the manufacturing cost increases. In addition, since the fine powder is easily splashed by a slight air flow, there is a problem that handling is difficult.

つぎに平均粒子径D50が異なる5種類の正極活物質材料をそれぞれ50mg取り出すとともに、その取り出した正極活物質材料に所定の圧力(例えば、6t/cm)を掛けてペレットに成形した。そして正極活物質材料の平均粒子径D50が異なる5種類のペレットをサンプルとして、各サンプルを焼成炉内に置いて熱収縮率を測定した。ここでは焼成炉内に100ml/minの流速で大気を導入しながら当該炉内を30℃から700℃まで100℃/hの速度で昇温させていったときの各サンプルの熱収縮率を熱機械分析装置(TMA)を用いて測定した。図2に各サンプルの熱収縮率の変化を示した。この図2では焼成炉内の昇温開始時点を起点とした経過時間(h)と、焼成炉内の温度(℃)および各サンプルのTMAの測定値(%)との関係が示されている。なおTMA測定値は、サンプルの体積変化率(%)を示しており、体積が膨張する場合はプラス「+」の数値となり、熱膨張率を示していることになる。収縮する場合はマイナス「−」の数値となり、その絶対値が熱収縮率となる。そして図示したように、各サンプルとも焼成炉内の温度が上昇するのに従って収縮し、また平均粒子径D50が小さなサンプルほど大きく収縮していることが確認できた。 Next, 50 mg of each of the five types of positive electrode active material having different average particle diameters D 50 was taken out, and the taken out positive electrode active material was subjected to a predetermined pressure (for example, 6 t / cm 2 ) to form a pellet. The average particle diameter D 50 of five different pellets of positive electrode active material as a sample was measured for thermal shrinkage rate at each sample in a firing furnace. Here, the heat shrinkage rate of each sample when the temperature in the furnace is raised from 30 ° C. to 700 ° C. at a rate of 100 ° C./h while introducing air into the firing furnace at a flow rate of 100 ml / min Measurements were made using a mechanical analyzer (TMA). FIG. 2 shows changes in the heat shrinkage rate of each sample. FIG. 2 shows the relationship between the elapsed time (h) starting from the temperature rising start time in the firing furnace, the temperature in the firing furnace (° C.), and the measured value (%) of TMA of each sample. . The TMA measurement value indicates the volume change rate (%) of the sample, and when the volume expands, it becomes a numerical value of plus “+” and indicates the thermal expansion coefficient. In the case of contraction, the value is minus “−”, and the absolute value is the thermal contraction rate. And as illustrated, contracts in accordance with the temperature in the firing furnace is increased in each sample, was also confirmed that the average particle diameter D 50 is greater shrinkage smaller the sample.

なお当然のことながら、積層電極体として焼結させる際にも、正極層内の電極活物質材料中に異相の結晶を混在させないようにする必要がある。すなわち上記製造工程における二次焼成の条件の範囲内で積層電極体を焼結させる必要がある。そして図2に示した平均粒子径D50が異なる電極活物質材料を含む各サンプルの体積変化率の時間変化と炉内温度の時間変化とから、各サンプルは結晶相が同相となる650℃〜680℃の温度範囲内で熱収縮していることが確認できる。したがって電極活物質材料の平均粒子径D50を1μm以上7μm以下に調整すれば、その電極活物質材料を用いることで全固体電池の容量を向上させることが期待できる。 Of course, it is necessary to prevent heterogeneous crystals from being mixed in the electrode active material in the positive electrode layer even when the laminated electrode body is sintered. That is, it is necessary to sinter the laminated electrode body within the range of the secondary firing conditions in the manufacturing process. And from the time change of the volume change rate of each sample and the time change of the furnace temperature of each sample containing the electrode active material having different average particle diameters D 50 shown in FIG. 2, each sample has a crystal phase in the same phase of 650 ° C. It can be confirmed that the heat shrinkage occurs within a temperature range of 680 ° C. Thus by adjusting the average particle diameter D 50 of the electrode active material to 1μm than 7μm or less, it can be expected to improve the capacity of the all-solid-state battery by using the electrode active material.

===その他の実施例===
本発明の実施例に係る全固体電池用正極活物質材料の製造方法では、LCPOからなる正極活物質材料を作製していたが、CoとNiとはその物性が近似しており、上記化学式LiMPにおいて、MをNiとした化合物や、MとしてCoとNiの双方を含む化合物であっても3個のLiが移動する多電子反応を示すため、その化合物を電極活物質として使用してもよい。
=== Other Embodiments ===
In the method for producing a positive electrode active material for an all solid state battery according to an embodiment of the present invention, a positive electrode active material made of LCPO was produced. However, Co and Ni have similar physical properties, and the chemical formula Li In 2 MP 2 O 7 , even if it is a compound in which M is Ni or a compound containing both Co and Ni as M, it shows a multi-electron reaction in which three Lis move, so that the compound is used as an electrode active material. May be used.

正極活物質自体をセラミック粉体の状態にしていたが、正極活物質の電子伝導性を向上させるためにセラミック粉体の粒子表面に、ジルコニア(ZrO)、アルミナ(Al)、チタン酸リチウム(LiTi12)、ニオブ酸リチウム(LiNbO)、炭素(C)などの導電剤をコーティングすることとしてもよい。導電剤を正極活物質材料にコーティングするためには、例えば、図1に示した製造手順において、一次焼成工程(s3)によって得られた粉体に導電剤の粉体を混合し、その混合物を二次焼成すればよい。 Although the positive electrode active material itself was in a ceramic powder state, zirconia (ZrO 2 ), alumina (Al 2 O 3 ), titanium was formed on the particle surface of the ceramic powder in order to improve the electronic conductivity of the positive electrode active material. lithium acid (Li 4 Ti 5 O 12) , lithium niobate (LiNbO 3), may be coated with a conductive agent such as carbon (C). In order to coat the conductive material on the positive electrode active material, for example, in the production procedure shown in FIG. 1, the powder of the conductive agent is mixed with the powder obtained by the primary firing step (s3), and the mixture is mixed. Secondary firing may be performed.

なおLiMPは、リチウム金属に対して5V程度の高い電位を示す。したがって、この対リチウム金属電位では、現在の非水電解液電池で使用されている有機電解液の多くが酸化分解してしまう。そのため現時点では、上記実施例の方法で作製された正極活物質材料を有機電解液を用いたリチウムイオン2次電池に使用することができない。しかし、今後、耐酸化性を有する電解液が生産された場合には、この当該材料を有機電解液を用いた電池にも使用できる。すなわち、本発明の適用範囲は、全固体電池のみに限定されず、電解液を用いたリチウム二次電池にも及んでいる。 Note that Li 2 MP 2 O 7 exhibits a high potential of about 5 V with respect to lithium metal. Therefore, at this potential against lithium metal, many of the organic electrolytes used in current non-aqueous electrolyte batteries are oxidatively decomposed. Therefore, at present, the positive electrode active material produced by the method of the above embodiment cannot be used for a lithium ion secondary battery using an organic electrolyte. However, when an electrolytic solution having oxidation resistance is produced in the future, this material can be used for a battery using an organic electrolytic solution. That is, the application range of the present invention is not limited to all solid state batteries, but extends to lithium secondary batteries using an electrolytic solution.

s2 混合工程、s3 一次焼成工程、s5 二次焼成工程   s2 mixing step, s3 primary firing step, s5 secondary firing step

Claims (3)

全固体電池用の正極活物質材料の製造方法であって、
化学式LiMPで表されるとともに、当該化学式中のMがCoとNiの一方あるいは双方を含む化合物からなる正極活物質の原材料を秤量して混合する混合ステップと、
前記混合ステップにより得た混合物を大気雰囲気中で仮焼成する一次焼成ステップと、
当該一次焼成ステップ後の前記混合物の粉体を当該一次焼成ステップよりも高い温度で大気雰囲気中で焼結させる二次焼成ステップと、
前記二次焼成ステップにより得た焼結体を粉砕する粉砕ステップと、
を含み、
前記二次焼成ステップでは、650℃以上680℃以下の温度で20時間以上30時間以下の時間で焼成すること、
を特徴とする全固体電池用正極活物質材料の製造方法としている。
A method for producing a positive electrode active material for an all-solid battery,
A mixing step of weighing and mixing the raw material of the positive electrode active material represented by the chemical formula Li 2 MP 2 O 7 , wherein M in the chemical formula is a compound containing one or both of Co and Ni;
A primary firing step in which the mixture obtained by the mixing step is temporarily fired in an air atmosphere;
A secondary firing step of sintering the powder of the mixture after the primary firing step in an air atmosphere at a temperature higher than the primary firing step;
A pulverizing step of pulverizing the sintered body obtained by the secondary firing step;
Including
In the secondary firing step, firing at a temperature of 650 ° C. to 680 ° C. for a time of 20 hours to 30 hours,
This is a method for producing a positive electrode active material for an all solid state battery.
請求項1において、前記粉砕ステップ、あるいは当該粉砕ステップによって得た粉砕物を解砕するステップを実行することで、1μm以上7μm以下の平均粒子径を有する正極活物質材料を得ることを特徴とする全固体電池用正極活物質材料の製造方法。   2. The positive electrode active material having an average particle diameter of 1 μm or more and 7 μm or less is obtained by executing the pulverization step or the step of pulverizing the pulverized material obtained by the pulverization step according to claim 1. A method for producing a positive electrode active material for an all solid state battery. 請求項1または2に記載の前記製造方法によって製造された全固体電池用正極活物質材料であって、LiMPで表されるとともに、当該化学式中のMがCoとNiの一方あるいは双方を含む化合物を含み、異相を含まない結晶構造を有する前記化合物の焼結体が粉体状に粉砕されてなることを特徴する全固体電池用正極活物質材料。 A positive electrode active material for all-solid-state battery manufactured by the manufacturing method according to claim 1 or 2, with represented by Li 2 MP 2 O 7, one M in the chemical formula of Co and Ni Alternatively, a positive electrode active material for an all-solid-state battery, wherein a sintered body of the compound having a crystal structure containing a compound containing both and having no heterogeneous phase is pulverized into a powder.
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JP2019169314A (en) * 2018-03-22 2019-10-03 Fdk株式会社 Method for producing positive electrode active material, positive electrode active material, and all-solid battery
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