JPH10233213A - Manufacture of secondary battery positive electrode active material - Google Patents

Manufacture of secondary battery positive electrode active material

Info

Publication number
JPH10233213A
JPH10233213A JP9032028A JP3202897A JPH10233213A JP H10233213 A JPH10233213 A JP H10233213A JP 9032028 A JP9032028 A JP 9032028A JP 3202897 A JP3202897 A JP 3202897A JP H10233213 A JPH10233213 A JP H10233213A
Authority
JP
Japan
Prior art keywords
active material
positive electrode
electrode active
fatty acid
secondary battery
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.)
Granted
Application number
JP9032028A
Other languages
Japanese (ja)
Other versions
JP3301335B2 (en
Inventor
Kazumi Okabe
参省 岡部
Yukio Sakabe
行雄 坂部
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Murata Manufacturing Co Ltd
Original Assignee
Murata Manufacturing Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Murata Manufacturing Co Ltd filed Critical Murata Manufacturing Co Ltd
Priority to JP03202897A priority Critical patent/JP3301335B2/en
Publication of JPH10233213A publication Critical patent/JPH10233213A/en
Application granted granted Critical
Publication of JP3301335B2 publication Critical patent/JP3301335B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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

Landscapes

  • Compositions Of Oxide Ceramics (AREA)
  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a manufacturing method by which a secondary battery positive electrode active material is manufactured at low costs and with high efficiency in which quality is uniform, sizes are fine, and filling density can be heightened. SOLUTION: In a manufacturing method for positive electrode active material shown by a general formula LiMx O2x (where M is an element of Ni, Mn, Co, Cr, Fe, or V, and (x) is 1 or 2), organic amine is added to mixture solution containing Li<+> and M<n+> (where (n) is the ion valence of M element) so as to precipitate M(OH)n , and hydrogen peroxide is added to M(OH)n formation solution so as to convert the M(OH)n into MOOH so as to precipitate Li2 O2 on MOOH particle surfaces. Li2 O2 -precipitated MOOH particles are dried, and MOOH powder is mixed into Li and M composite fatty acid metal salt compound solution. Thereafter, the same is dried so as to coat the surface of the powder by the Li and M composite fatty acid metal salt compound, and the coated powder is heat treated.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、一般式LiMx O
2x(但し、MはNi、Mn、Co、Cr、Fe及びVか
ら選ばれた少なくとも1種の元素であり、xは1又は2
である)で表される二次電池用正極活物質の製造方法に
関する。
The present invention relates to a compound of the general formula LiM x O
2x (where M is at least one element selected from Ni, Mn, Co, Cr, Fe and V, x is 1 or 2
The present invention relates to a method for producing a positive electrode active material for a secondary battery represented by

【0002】[0002]

【従来の技術】従来、二次電池用正極活物質の製造方法
としては、次のような方法が提案されている。
2. Description of the Related Art Conventionally, the following method has been proposed as a method for producing a positive electrode active material for a secondary battery.

【0003】(1)二次電池用正極活物質を構成する金
属元素イオンの炭酸塩又は酸化物の粉体を別々に秤量
し、それらを混合粉砕して700℃以上の温度で仮焼し
て目的の二次電池用正極活物質を得る。
(1) Powders of carbonates or oxides of metal element ions constituting the positive electrode active material for secondary batteries are separately weighed, mixed and pulverized, and calcined at a temperature of 700 ° C. or more. A desired positive electrode active material for a secondary battery is obtained.

【0004】(2)アルコキシドを用いるゾル−ゲル法
により二次電池用正極活物質を得る。
(2) A positive electrode active material for a secondary battery is obtained by a sol-gel method using an alkoxide.

【0005】(3)二次電池用正極活物質を構成する金
属元素イオンの混合溶液に沈殿を形成させる沈殿剤を添
加反応させ、得られた沈殿を仮焼して目的の二次電池用
正極活物質を得る。
(3) A precipitant for forming a precipitate is added to a mixed solution of metal element ions constituting the positive electrode active material for a secondary battery to cause a reaction, and the obtained precipitate is calcined to obtain a desired positive electrode for a secondary battery. Obtain the active material.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上記の
製造方法それぞれにおいて、以下に示すような問題点を
有していた。
However, each of the above-described manufacturing methods has the following problems.

【0007】(1)の方法では、出発原料として炭酸塩
又は酸化物の粉体を使用するため、各々の粉体を分子レ
ベルで均一に混合することは不可能である。このため、
局部的な組成ずれが生じ、均質な正極活物質を得ること
ができない。
In the method (1), since a carbonate or oxide powder is used as a starting material, it is impossible to uniformly mix each powder at a molecular level. For this reason,
Local composition deviation occurs, and a uniform positive electrode active material cannot be obtained.

【0008】なお。出発原料である各粉体は湿式法で合
成し、その沈殿物を仮焼することによっても製造でき
る。しかしながら、合成時の沈殿物が微細であっても、
使用する際に乾燥などの処理を行なうため凝集して粒子
が粗大化し、表面活性が悪くなるため、二次電池用の正
極活物質を得るためには700℃以上の高温で仮焼する
必要がある。そして、このように高温で仮焼して得た仮
焼粉体は粒子が強く凝集して粗大化しているため、充填
密度が低く表面積が小さくなり、二次電池の正極活物質
として用いた場合、十分な電気量を取り出すことができ
ない。
[0008] Incidentally. Each powder as a starting material can be synthesized by a wet method and then calcined to precipitate. However, even if the precipitate during synthesis is fine,
When used, a treatment such as drying is performed to agglomerate and coarsen particles, resulting in poor surface activity. Therefore, in order to obtain a positive electrode active material for a secondary battery, it is necessary to calcine at a high temperature of 700 ° C. or more. is there. The calcined powder obtained by calcining at a high temperature in this way has a low packing density and a small surface area because the particles are strongly agglomerated and coarse, and when used as a positive electrode active material of a secondary battery. , Can not take out enough electricity.

【0009】(2)の方法では、低温で目的とする二次
電池用の正極活物質を合成でき、かつ得られる正極活物
質粉体の粒径が微細で比表面積が大きく充填密度が高く
なるので、二次電池の正極活物質として用いた場合、電
気量を十分に取り出すことができるという利点がある。
しかしながら、出発原料であるアルコキシドは実験室的
には適した材料ではあるが、工業的には高価過ぎて採用
できない。
In the method (2), the desired cathode active material for a secondary battery can be synthesized at a low temperature, and the obtained cathode active material powder has a fine particle size, a large specific surface area, and a high packing density. Therefore, when used as a positive electrode active material of a secondary battery, there is an advantage that a sufficient amount of electricity can be taken out.
However, although the alkoxide as a starting material is a material suitable for a laboratory, it is too expensive for industrial use and cannot be used.

【0010】又、アルコキシドは水分に対して非常に敏
感で加水分解しやすいため、空気中の水分の影響を受け
ないような反応装置を必要とし、設備費が高くなりコス
トアップの要因となる。
Further, alkoxides are very sensitive to water and are easily hydrolyzed. Therefore, a reactor is required which is not affected by water in the air, which increases equipment costs and causes cost increase.

【0011】(3)の方法としては、例えば、蓚酸塩と
して沈殿物を形成した後仮焼して目的の二次電池用正極
活物質を得る方法がある。この方法は、(1)の方法に
比べると構成元素の分散性が格段に改良されている。
As the method (3), for example, there is a method in which a precipitate is formed as an oxalate and then calcined to obtain a desired cathode active material for a secondary battery. In this method, the dispersibility of the constituent elements is significantly improved as compared with the method (1).

【0012】しかしながら、蓚酸塩沈殿物は、水に対し
て溶解度の低い化合物もあるが、一般的には水に対して
かなり高い溶解度を有しているのが普通である。したが
って、二次電池用正極活物質を構成する各元素の蓚酸塩
化合物の溶解度に差が生じ、洗浄・脱水後における沈殿
物の構成元素比率が仕込み時と異なってくるという問題
点を有している。
However, oxalate precipitates have low solubility in some compounds, but generally have rather high solubility in water. Therefore, there is a problem that a difference occurs in the solubility of the oxalate compound of each element constituting the positive electrode active material for a secondary battery, and the constituent element ratio of the precipitate after washing and dehydration is different from that at the time of preparation. I have.

【0013】又、Liと他の構成元素の沈殿物を同時に
得るための沈殿形成剤がないという問題がある。例え
ば、Li以外の構成元素は苛性アルカリ炭酸塩を沈殿形
成剤に用いることで難溶性の水酸化物又は炭酸塩の沈殿
を形成することが可能であるが、Liの水酸化物や炭酸
塩は水に対して易溶性であるので、沈殿物として得るこ
とができない。
Another problem is that there is no precipitation-forming agent for simultaneously obtaining a precipitate of Li and other constituent elements. For example, the constituent elements other than Li can form a precipitate of a hardly soluble hydroxide or carbonate by using caustic alkali carbonate as a precipitation-forming agent, but the hydroxide or carbonate of Li is Since it is easily soluble in water, it cannot be obtained as a precipitate.

【0014】そこで、本発明の目的は、上述の問題点を
解決して、均質、微細であって充填密度を高めることが
できる、二次電池用の正極活物質を安価に効率よく製造
する方法を提供することにある。
Accordingly, an object of the present invention is to provide a method for efficiently and inexpensively producing a positive electrode active material for a secondary battery which solves the above-mentioned problems and is homogeneous, fine and capable of increasing the packing density. Is to provide.

【0015】[0015]

【課題を解決するための手段】上記目的を達成するた
め、本発明の二次電池用正極活物質の製造方法は、一般
式LiMx O2x(但し、MはNi、Mn、Co、Cr、
Fe及びVから選ばれた少なくとも1種の元素であり、
xは1又は2である)で示される二次電池用正極活物質
の製造方法において、Li+ 及びMn+(但し、nはM元
素のイオン価数を示す)を含む混合溶液に有機アミンを
加えてM(OH)n (但し、nはM元素のイオン価数を
示す)を沈殿させる工程と、該M(OH)n 生成溶液に
過酸化水素を加えてM(OH)n をMOOHにするとと
もに該MOOH粒子表面にLi2 O2 を沈着させる工程
と、該Li2 O2 が沈着したMOOH粒子を乾燥させる
工程と、該MOOHの粉体をLi及びMの複合脂肪酸金
属塩化合物の溶液と混合した後、乾燥させて前記粉体の
表面をLi及びMの複合脂肪酸金属塩化合物で被覆する
工程と、該被覆された粉体を熱処理する工程と、を備え
たことを特徴とする。
In order to achieve the above object, a method for producing a positive electrode active material for a secondary battery according to the present invention comprises a general formula LiM x O 2x (where M is Ni, Mn, Co, Cr,
At least one element selected from Fe and V,
x is 1 or 2), wherein an organic amine is added to a mixed solution containing Li + and M n + (where n represents the ionic valence of M element). In addition, a step of precipitating M (OH) n (where n represents the ionic valence of the M element), and adding hydrogen peroxide to the M (OH) n producing solution to convert M (OH) n to MOOH. And depositing Li 2 O 2 on the surface of the MOOH particles, drying the MOOH particles having the Li 2 O 2 deposited thereon, and dissolving the MOOH powder in a solution of a complex fatty acid metal salt compound of Li and M. And a step of drying and coating the surface of the powder with a complex fatty acid metal salt compound of Li and M, and a step of heat-treating the coated powder.

【0016】又、前記M元素のイオン源は、水溶性化合
物又は硝酸若しくは酢酸に溶解する化合物であることを
特徴とする。
Further, the ion source of the element M is a water-soluble compound or a compound soluble in nitric acid or acetic acid.

【0017】又、前記アミンを加えたとき、pHを9〜
9.5に調整することを特徴とする。
When the amine is added, the pH is adjusted to 9 to
It is characterized in that it is adjusted to 9.5.

【0018】又、前記複合脂肪酸金属塩化合物で被覆さ
れた粉体の熱処理温度は、450〜650℃であること
を特徴とする。
The heat treatment temperature of the powder coated with the complex fatty acid metal salt compound is 450 to 650 ° C.

【0019】さらに、前記複合脂肪酸金属塩化合物は、
炭素数5〜30の直鎖飽和脂肪酸又はモノエン不飽和脂
肪酸とLi及びM元素の酢酸塩とを反応させて得られた
ものであることを特徴とする。
Further, the complex fatty acid metal salt compound is
It is obtained by reacting a linear saturated fatty acid or monoene unsaturated fatty acid having 5 to 30 carbon atoms with an acetate of Li and M elements.

【0020】ここで、Li+ の原料としては、水酸化リ
チウム、酢酸リチウム、炭酸リチウム、硝酸リチウムな
どが挙げられるがこれらの化合物に限定されるものでは
ない。水溶性又は酢酸若しくは硝酸に可溶な化合物を適
宜用いることができる。
Here, examples of the raw material of Li + include lithium hydroxide, lithium acetate, lithium carbonate, lithium nitrate and the like, but are not limited to these compounds. A compound that is water-soluble or soluble in acetic acid or nitric acid can be used as appropriate.

【0021】又、Mn+の原料としても、Liの場合と同
じく水酸化物、酢酸塩、炭酸塩、硝酸塩などが挙げられ
るがこれらの化合物に限定されるものではない。水溶性
又は酢酸若しくは硝酸に可溶な化合物を適宜用いること
が可能である。
The raw materials of M n + include hydroxides, acetates, carbonates, nitrates and the like as in the case of Li, but are not limited to these compounds. A compound that is water-soluble or soluble in acetic acid or nitric acid can be used as appropriate.

【0022】又、複合脂肪酸金属塩化合物を得るために
用いる直鎖飽和脂肪酸としては、ヘキサン酸、オクタン
酸、ノナン酸、デカン酸、ウンデカン酸、ドデカン酸、
テトラデカン酸、ヘキサデカン酸、オクタデカン酸、エ
イコサン酸、ドコサン酸、テトラコサン酸、ヘキサコサ
ン酸、オクタコサン酸、トリアコン酸などが挙げられ
る。
The straight-chain saturated fatty acids used for obtaining the complex fatty acid metal salt compound include hexanoic acid, octanoic acid, nonanoic acid, decanoic acid, undecanoic acid, dodecanoic acid, and the like.
Examples include tetradecanoic acid, hexadecanoic acid, octadecanoic acid, eicosanoic acid, docosanoic acid, tetracosanoic acid, hexacosanoic acid, octacosanoic acid, and triaconic acid.

【0023】さらに、モノエン不飽和脂肪酸としては、
cis−4−デセン酸、9−デセン酸、cis−4−ド
デセン酸、10−ウンデセン酸、cis−4−テトラデ
セン酸、cis−5−テロラデセン酸、cis−9−テ
トラデセン酸、cis−6−ヘキサデセン酸、cis−
9−ヘキサデセン酸、cis−6−オクタデセン酸、c
is−9−オクタデセン酸、trans−9−オクタデ
セン酸、cis−11−オクタデセン酸、trans−
11−オクタデセン酸、cis−9−エイコセン酸、c
is−11−ドコセン酸、cis−13−ドコセン酸、
trans−13−ドコセン酸、cis−15−テトラ
コセン酸、cis−17−ヘキサコセン酸、cis−2
1−トリアコンテン酸などが挙げられる。
Further, as the monoene unsaturated fatty acid,
cis-4-decenoic acid, 9-decenoic acid, cis-4-dodecenoic acid, 10-undecenoic acid, cis-4-tetradecenoic acid, cis-5-teradedecenoic acid, cis-9-tetradecenoic acid, cis-6-hexadecene Acid, cis-
9-hexadecenoic acid, cis-6-octadecenoic acid, c
is-9-octadecenoic acid, trans-9-octadecenoic acid, cis-11-octadecenoic acid, trans-
11-octadecenoic acid, cis-9-eicosenoic acid, c
is-11-docosenoic acid, cis-13-docosenoic acid,
trans-13-docosenoic acid, cis-15-tetracosenoic acid, cis-17-hexacosenic acid, cis-2
1-triacontenic acid and the like.

【0024】上述のように、本発明は、MOOHという
ヒドロキシ酸化物沈殿粒子の表面に、水に対して不溶性
のLi2 O2 を沈着させた2重構造の沈殿粒子の形成方
法を採用している。このため、Li化合物の溶解により
構成元素比率が仕込み時と異なることはない。又、正極
活物質を構成する元素化合物が互いに直接接触して構成
元素同士が最短距離にあるため、相互の反応がスムーズ
に進行しやすい。これにより、従来の固相法による方法
よりも低温の450〜650℃で二次電池用正極活物質
を得ることができる。そして、分散性に優れた二次電池
用正極活物質を得ることができる。
As described above, the present invention employs a method of forming precipitated particles having a double structure in which water-insoluble Li 2 O 2 is deposited on the surface of hydroxy oxide precipitated particles of MOOH. I have. For this reason, the constituent element ratio does not differ from that at the time of preparation due to dissolution of the Li compound. In addition, since the element compounds constituting the positive electrode active material are in direct contact with each other and the constituent elements are at the shortest distance, the mutual reaction tends to proceed smoothly. As a result, a positive electrode active material for a secondary battery can be obtained at a lower temperature of 450 to 650 ° C. than the conventional solid phase method. And the positive electrode active material for secondary batteries which is excellent in dispersibility can be obtained.

【0025】なお、MOOH沈殿粒子表面にLi2 O2
を沈着させた二重構造の粉体は、大気中に放置するとL
i2 O2 が水分を吸収して粉体自体が湿って取扱い性が
悪くなるという欠点を有している。このLi2 O2 の吸
湿性を防止する対策として、高級脂肪酸などの撥水性の
化合物でさらにLi2 O2 表面を覆うことが考えられ
る。しかしながら、高級脂肪酸そのものはLi2 O2 と
反応してLiの脂肪酸塩を生成し、Li2 O2 を溶解す
るため好ましくない。本発明においては、正極活物資を
構成するLi及びMの複合脂肪酸金属塩化合物で被覆す
ることで、Li2O2 との反応を防いで吸湿性を防止し
ている。又、撥水性を持たせるために被覆する複合脂肪
酸金属塩化合物のLiとMの比率を、Li2 O2 とMO
OH即ち目的とするLiMx O2xのLiとMの比率に合
わせることにより、異なる組成の物質を生成することは
なく、均質な特性の安定した二次電池用正極活物質を得
ることができる。
The surface of the MOOH precipitated particles has Li 2 O 2
The double-structured powder deposited with
There is a disadvantage that i 2 O 2 absorbs moisture and the powder itself becomes wet, resulting in poor handling. The Li as a countermeasure for preventing hygroscopic 2 O 2, it is conceivable to cover the Li 2 O 2 surface with a compound of the water-repellent higher fatty acid. However, higher fatty acids themselves are not preferable because they react with Li 2 O 2 to form a fatty acid salt of Li and dissolve Li 2 O 2 . In the present invention, by covering with a complex fatty acid metal salt compound of Li and M constituting the positive electrode active material, the reaction with Li 2 O 2 is prevented and the hygroscopicity is prevented. In addition, the ratio of Li and M of the complex fatty acid metal salt compound to be coated for imparting water repellency is determined by comparing Li 2 O 2 and MO
By matching the OH i.e. LiM x O 2x of Li and the ratio of M of interest, rather than generating a material of a different composition, it is possible to obtain a stable cathode active material for a secondary battery was homogeneous properties.

【0026】なお、複合脂肪酸金属塩化合物そのものの
熱分解温度は450〜500℃である。ところが、MO
OH及びLi2 O2 が共存すると、MOOH及びLi2
O2の熱分解時に放出される発生期の酸素の作用によっ
て複合脂肪酸金属塩化合物の燃焼が促進され、単独で熱
分解させるよりも200℃以上も低い250〜270℃
という温度で分解燃焼が起こる。そして、この複合脂肪
酸金属塩化合物の燃焼熱によって、さらに低温でLiM
x O2xが生成する。
The thermal decomposition temperature of the complex fatty acid metal salt compound itself is 450 to 500 ° C. However, MO
When OH and Li 2 O 2 coexist, MOOH and Li 2
Combustion of the complex fatty acid metal salt compound is promoted by the action of nascent oxygen released at the time of thermal decomposition of O 2, and the temperature is 250 to 270 ° C., which is 200 ° C. or more lower than that of the case of thermal decomposition alone
Decomposition combustion occurs at such a temperature. Then, the heat of combustion of the complex fatty acid metal salt compound causes the LiM
x O 2x is produced.

【0027】又、二次電池用正極活物質の出発原料とし
て、水溶性化合物又は硝酸若しくは酢酸に可溶な水酸化
物、酢酸塩、炭酸塩、硝酸塩などを用いるのため、安価
な二次電池用正極活物質を得ることができる。
In addition, since a water-soluble compound or a hydroxide, acetate, carbonate, nitrate or the like soluble in nitric acid or acetic acid is used as a starting material of the positive electrode active material for a secondary battery, an inexpensive secondary battery is used. The positive electrode active material for use can be obtained.

【0028】[0028]

【発明の実施の形態】以下、本発明の二次電池用正極活
物質の製造方法の実施の形態について、実施例に基づき
説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the method for producing a positive electrode active material for a secondary battery according to the present invention will be described below based on examples.

【0029】(実施例)まず、出発原料として酢酸リチ
ウム、酢酸マンガン及び酢酸コバルトを用意した。次
に、Li、Mn及びCoが表1の試料番号1〜3に示す
比率になるように、用意した出発原料を正確に秤量分取
した後、純水中に入れて高速で攪拌して溶解させて、L
i+ 及びMn+(但し、MはMn又はCo)を含む混合溶
液を調整した。なお、混合溶液の濃度は、目的とする正
極活物質に換算で0.1mol/Lになるようにした。
その後、この混合溶液を高速攪拌しながら、ジメチルア
ミン水溶液を加えてpHを9〜9.5に調節し、まずM
(OH)n の沈殿粒子を生成させた。さらに、(Li+
+Mn+)の合計当量と同当量のH2 O2 水(30%濃
度)を高速攪拌しながらゆっくりと加えて、M(OH)
n を酸化してMOOHにすると共にLi+ をLi2 O2
の沈殿としてMOOH沈殿粒子表面に沈着させた。その
後、沈殿生成物を有する反応液をロータリーエバポレー
タに移し、50mmHgの減圧、加熱温度60℃の条件
で溶媒を除去して乾燥粉体を得た。
(Example) First, lithium acetate, manganese acetate and cobalt acetate were prepared as starting materials. Next, after accurately weighing and dispensing the prepared starting materials so that the ratios of Li, Mn and Co are as shown in Sample Nos. 1 to 3 in Table 1, dissolve them in pure water by stirring at high speed. Let L
A mixed solution containing i + and M n + (where M is Mn or Co) was prepared. The concentration of the mixed solution was adjusted to 0.1 mol / L in terms of the target positive electrode active material.
Thereafter, while the mixed solution was stirred at a high speed, an aqueous dimethylamine solution was added to adjust the pH to 9 to 9.5.
(OH) n precipitated particles were formed. Furthermore, (Li +
+ M n + ) was slowly added with high-speed stirring to the same equivalent of H 2 O 2 water (30% concentration) to obtain M (OH)
n is oxidized to MOOH and Li + is converted to Li 2 O 2
Was deposited on the surface of the MOOH precipitated particles. Thereafter, the reaction solution having the precipitated product was transferred to a rotary evaporator, and the solvent was removed under the conditions of a reduced pressure of 50 mmHg and a heating temperature of 60 ° C. to obtain a dry powder.

【0030】[0030]

【表1】 [Table 1]

【0031】次に、得られた乾燥粉体を、この粉体の1
2.5wt%に相当する量の撥水性の複合脂肪酸金属塩
化合物を溶解させたベンゼン溶液中に入れ混合した。そ
の後、過剰のベンゼンを加熱蒸発させて除去し、乾燥粉
体の表面を複合脂肪酸金属塩化合物で被覆した。
Next, the obtained dried powder is mixed with 1
A water-repellent complex fatty acid metal salt compound in an amount corresponding to 2.5 wt% was placed in a benzene solution in which it was dissolved and mixed. Thereafter, excess benzene was removed by heating and evaporating, and the surface of the dried powder was covered with a complex fatty acid metal salt compound.

【0032】なお、複合脂肪族金属塩化合物は、酢酸リ
チウム、酢酸マンガン及び酢酸コバルトを、Li、Mn
及びCoが表1のそれぞれ試料番号1〜3に示す比率と
なるように分取し、これに直鎖飽和脂肪酸としてのオク
タデカン酸を加えたものをベンゼン溶液中で分散加熱し
ながら反応させて合成したものを用いた。
The complex aliphatic metal salt compound is prepared by converting lithium acetate, manganese acetate and cobalt acetate into Li, Mn.
And Co were collected so as to have the ratios shown in Sample Nos. 1 to 3 in Table 1, and octadecanoic acid as a linear saturated fatty acid was added thereto and reacted while dispersing and heating in a benzene solution. What was done was used.

【0033】次に、Li2 O2 が沈着したMOOH粒子
表面を複合脂肪酸金属塩化合物で被覆した粉体を250
〜700℃の温度で2時間熱処理した。
Next, powder obtained by coating the surface of the MOOH particles on which Li 2 O 2 is deposited with a complex fatty acid metal salt compound
Heat treatment was performed at a temperature of 700700 ° C. for 2 hours.

【0034】その後、得られた熱処理粉体をX線回折
(XRD)分析して生成物を同定すると共に、走査型電
子顕微鏡(SEM)観察により粒径を求めた。その結果
を表2に示す。なお、表2中、LM1 はLiMnO2 を
表し、LCはLiCoO2 を表し、LM2 はLiMn2
O4 を表す。そして、Lx Cy はx/y=1.00でな
いLi−Co系の酸化物を表し、LM1#、LM2#及びL
C# は生成開始直後の結晶性のあまいLM1 、LM2 及
びLCを表す。
Thereafter, the obtained heat-treated powder was analyzed by X-ray diffraction (XRD) to identify the product, and the particle size was determined by observation with a scanning electron microscope (SEM). Table 2 shows the results. In Table 2, LM 1 represents LiMnO 2 , LC represents LiCoO 2 , and LM 2 represents LiMn 2
Represents O 4 . Then, L x C y represents an oxide of Li-Co-based non-x / y = 1.00, LM 1 #, LM 2 # and L
C # represents sweet LM 1, LM 2 and LC-crystalline immediately after generation starts.

【0035】[0035]

【表2】 [Table 2]

【0036】(比較例)Li及Coが表1の比較例に示
す比率になるように、炭酸リチウムと酸化コバルトの粉
体を正確に秤量分取してポリエチレン製ポットに入れエ
タノールを加えて混合粉砕した後、550〜750℃で
2時間熱処理を行ない熱処理粉体を得た。
(Comparative Example) Lithium carbonate and cobalt oxide powders were accurately weighed and weighed and placed in a polyethylene pot, and ethanol was added and mixed so that the ratio of Li and Co was as shown in the comparative example in Table 1. After pulverization, heat treatment was performed at 550 to 750 ° C. for 2 hours to obtain a heat-treated powder.

【0037】その後、得られた熱処理粉体をXRD分析
して生成物の同定を行なった。その結果を表2に示す。
Thereafter, the obtained heat-treated powder was subjected to XRD analysis to identify the product. Table 2 shows the results.

【0038】表2の結果から明らかなように、比較例で
は熱処理温度が750℃以上にならないとLiCoO2
の単層の粉体が得られないのに対して、実施例では45
0℃ですでにLiCoO2 の単層の粉体が得られてい
て、従来方法よりも300℃も低い温度で目的の二次電
池用正極活物質が得られている。又、LiMnO2 やL
iMn2 O4 についても、450℃という低い熱処理温
度で単層の化合物が得られてる。又、本実施例で得られ
る二次電池用正極活物質の粉体の平均粒径は、約0.3
μmとサブミクロンオーダーの微細なものである。
As is clear from the results in Table 2, in the comparative example, the LiCoO 2
Whereas a single-layer powder of
At 0 ° C., a single-layer powder of LiCoO 2 has already been obtained, and the desired positive electrode active material for a secondary battery has been obtained at a temperature lower by 300 ° C. than the conventional method. Also, LiMnO 2 or L
Also for iMn 2 O 4 , a single layer compound was obtained at a heat treatment temperature as low as 450 ° C. The average particle size of the powder of the positive electrode active material for a secondary battery obtained in this example was about 0.3.
It is as fine as μm and submicron order.

【0039】以上の結果より、本発明の方法によれば、
均質、微細であって、二次電池の正極活物質として用い
た場合に充填密度を高めることができるLiCoO2 、
LiMnO2 及びLiMn2 O4 の粉体を得ることがで
きる。
From the above results, according to the method of the present invention,
LiCoO 2 , which is homogeneous and fine and can increase the packing density when used as a positive electrode active material of a secondary battery,
Powders of LiMnO 2 and LiMn 2 O 4 can be obtained.

【0040】なお、上記実施例においては、出発原料が
酢酸塩の場合について説明したが、本発明はこれのみに
限定されるものではない。水酸化物、酢酸塩、炭酸塩、
硝酸塩など、水溶性化合物又は硝酸若しくは酢酸に溶解
する化合物を適宜用いることができる。
In the above embodiment, the case where the starting material is an acetate is described, but the present invention is not limited to this. Hydroxides, acetates, carbonates,
A water-soluble compound such as a nitrate or a compound soluble in nitric acid or acetic acid can be used as appropriate.

【0041】又、複合脂肪酸金属塩化合物は、酢酸塩と
直鎖飽和脂肪酸の1種であるオクタデカン酸とを反応さ
せて得たが、炭素数5〜30の他の直鎖飽和脂肪酸やモ
ノエン不飽和脂肪酸と酢酸塩とを反応させても得ること
ができる。
The complex fatty acid metal salt compound was obtained by reacting an acetate with octadecanoic acid, which is a kind of linear saturated fatty acid. It can also be obtained by reacting a saturated fatty acid with an acetate.

【0042】さらに、上記実施例においては、正極活物
質がLiCoO2 、LiMnO2 又はLiMn2 O4 の
場合について説明したが、本発明はこれのみに限定され
るものではない。一般式LiMx O2x(但し、MはN
i、Mn、Co、Cr、Fe及びVから選ばれた少なく
とも1種の元素であり、xは1又は2である)で示され
る正極活物質についても、同様に、均質、微細な粉体を
得ることができる。
Further, in the above embodiment, the case where the positive electrode active material is LiCoO 2 , LiMnO 2 or LiMn 2 O 4 has been described, but the present invention is not limited to this. General formula LiM x O 2x (where M is N
i, Mn, Co, Cr, Fe and V, and at least one element selected from x, and x is 1 or 2). Obtainable.

【0043】[0043]

【発明の効果】以上の説明から明らかなように、本発明
によれば、均質な二次電池用正極活物質を低温で合成す
ることができる。そして、得られる正極活物質の粒子径
はサブミクロンと微細である。
As is clear from the above description, according to the present invention, a homogeneous cathode active material for a secondary battery can be synthesized at a low temperature. The obtained positive electrode active material has a submicron particle size.

【0044】したがって、本発明により得られる正極活
物質を二次電池に用いることにより、正極活物質の充填
密度を高めて電気容量を増大させることができる。
Therefore, by using the positive electrode active material obtained by the present invention in a secondary battery, the packing density of the positive electrode active material can be increased and the electric capacity can be increased.

【0045】さらに、出発原料として安価な無機酸塩を
用いること、粉砕工程等を必要としないことなどによ
り、二次電池用正極活物質を工業的に安価に製造するこ
とができる。
Further, the use of an inexpensive inorganic acid salt as a starting material and the elimination of a pulverizing step and the like make it possible to industrially produce a positive electrode active material for a secondary battery at low cost.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 一般式LiMx O2x(但し、MはNi、
Mn、Co、Cr、Fe及びVから選ばれた少なくとも
1種の元素であり、xは1又は2である)で示される二
次電池用正極活物質の製造方法において、Li+ 及びM
n+(但し、nはM元素のイオン価数を示す)を含む混合
溶液に有機アミンを加えてM(OH)n (但し、nはM
元素のイオン価数を示す)を沈殿させる工程と、該M
(OH)n 生成溶液に過酸化水素を加えてM(OH)n
をMOOHにするとともに該MOOH粒子表面にLi2
O2 を沈着させる工程と、該Li2 O2 が沈着したMO
OH粒子を乾燥させる工程と、該MOOHの粉体をLi
及びMの複合脂肪酸金属塩化合物の溶液と混合した後、
乾燥させて前記粉体の表面をLi及びMの複合脂肪酸金
属塩化合物で被覆する工程と、該被覆された粉体を熱処
理する工程と、を備えたことを特徴とする二次電池用正
極活物質の製造方法。
1. The general formula LiM x O 2x (where M is Ni,
Mn, Co, Cr, at least one element selected from Fe and V, x in the positive electrode active material manufacturing method of the secondary battery represented by 1 or 2), Li + and M
An organic amine is added to a mixed solution containing n + (where n represents the ionic valence of M element) to form M (OH) n (where n is M
Precipitating the ionic valence of the element);
Hydrogen peroxide is added to the (OH) n producing solution to form M (OH) n
To MOOH, and Li 2
The step of depositing O 2 and the MO on which the Li 2 O 2 is deposited.
Drying the OH particles;
And after mixing with the solution of the complex fatty acid metal salt compound of M
A step of drying and coating the surface of the powder with a complex fatty acid metal salt compound of Li and M; and a step of heat-treating the coated powder. The method of manufacturing the substance.
【請求項2】 前記M元素のイオン源は、水溶性化合物
又は硝酸若しくは酢酸に溶解する化合物であることを特
徴とする、請求項1記載の二次電池用正極活物質の製造
方法。
2. The method according to claim 1, wherein the ion source of the element M is a water-soluble compound or a compound soluble in nitric acid or acetic acid.
【請求項3】 前記アミンを加えたとき、pHを9〜
9.5に調整することを特徴とする、請求項1記載の二
次電池用正極活物質の製造方法。
3. When the amine is added, the pH is adjusted to 9 to 9.
The method for producing a positive electrode active material for a secondary battery according to claim 1, wherein the method is adjusted to 9.5.
【請求項4】 前記複合脂肪酸金属塩化合物で被覆され
た粉体の熱処理温度は、450〜650℃であることを
特徴とする、請求項1記載の二次電池用正極活物質の製
造方法。
4. The method according to claim 1, wherein the heat treatment temperature of the powder coated with the complex fatty acid metal salt compound is 450 to 650 ° C.
【請求項5】 前記複合脂肪酸金属塩化合物は、炭素数
5〜30の直鎖飽和脂肪酸又はモノエン不飽和脂肪酸と
Li及びM元素の酢酸塩とを反応させて得られたもので
あることを特徴とする、請求項1〜4のいずれかに記載
の二次電池用正極活物質の製造方法。
5. The complex fatty acid metal salt compound is obtained by reacting a linear saturated fatty acid having 5 to 30 carbon atoms or a monoene unsaturated fatty acid with acetates of Li and M elements. The method for producing a positive electrode active material for a secondary battery according to claim 1.
JP03202897A 1997-02-17 1997-02-17 Method for producing positive electrode active material for secondary battery Expired - Fee Related JP3301335B2 (en)

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