JP2000264638A - Method for producing lithium manganese composite oxide for lithium secondary battery positive electrode active material - Google Patents
Method for producing lithium manganese composite oxide for lithium secondary battery positive electrode active materialInfo
- Publication number
- JP2000264638A JP2000264638A JP11078408A JP7840899A JP2000264638A JP 2000264638 A JP2000264638 A JP 2000264638A JP 11078408 A JP11078408 A JP 11078408A JP 7840899 A JP7840899 A JP 7840899A JP 2000264638 A JP2000264638 A JP 2000264638A
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- Prior art keywords
- composite oxide
- lithium
- manganese composite
- positive electrode
- aqueous solution
- Prior art date
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Battery Electrode And Active Subsutance (AREA)
- Compounds Of Iron (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Secondary Cells (AREA)
Abstract
(57)【要約】
【課題】 リチウム二次電池用正極活物質となり得るス
ピネル構造リチウムマンガン複合酸化物の製造方法であ
って、結晶組成の均一性に優れたリチウムマンガン複合
酸化物を、簡便かつ低コストに製造できる方法を提供す
る
【解決手段】 マンガン源あるいはマンガンおよびマン
ガンサイトを置換可能な他元素源となる硝酸塩水溶液
と、リチウム源またはリチウムおよびリチウムサイトを
置換可能なアルカリ金属元素源となる水酸化物のH2O2
水溶液とを混合し、溶液反応によって、層状岩塩構造の
複合酸化物前駆体を析出させる析出工程と、析出した前
駆体を比較的低温度中に保持して熟成させ、結晶構造を
層状岩塩構造からスピネル構造へ転移させる熟成工程と
から構成する。PROBLEM TO BE SOLVED: To provide a method for producing a lithium manganese composite oxide having a spinel structure, which can be used as a positive electrode active material for a lithium secondary battery, in a simple and easy manner. Provided is a method capable of producing at low cost. A nitrate aqueous solution serving as a manganese source or another element source capable of replacing manganese and manganese sites, and a lithium source or an alkali metal element source capable of replacing lithium and lithium sites are provided. Hydroxide H 2 O 2
An aqueous solution is mixed, and a solution reaction is performed to deposit a composite oxide precursor having a layered rock salt structure, and the deposited precursor is kept at a relatively low temperature and aged to change the crystal structure from the layered rock salt structure. And a ripening step of transferring to a spinel structure.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、リチウムイオンの
吸蔵・放出現象を利用したリチウム二次電池の正極活物
質となるリチウムマンガン複合酸化物の製造方法に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a lithium manganese composite oxide as a positive electrode active material of a lithium secondary battery utilizing a phenomenon of insertion and extraction of lithium ions.
【0002】[0002]
【従来の技術】携帯電話、パソコン等の小型化に伴い、
エネルギー密度の高い二次電池が必要とされ、通信機
器、情報関連機器の分野では、リチウム二次電池が広く
普及するに至っている。また、資源問題、環境問題か
ら、自動車の分野でも電気自動車に対する要望が高ま
り、安価であってかつ容量が大きく、サイクル特性が良
好なリチウム二次電池の開発が急がれている。2. Description of the Related Art As mobile phones and personal computers become smaller,
Secondary batteries with high energy density are required, and lithium secondary batteries have come into widespread use in the fields of communication devices and information-related devices. In addition, demands for electric vehicles are increasing in the field of automobiles due to resource problems and environmental problems, and the development of lithium secondary batteries that are inexpensive, have large capacities, and have good cycle characteristics is urgently required.
【0003】現在、リチウム二次電池の正極活物質に
は、4V級の二次電池を構成できるものとして、規則配
列層状岩塩構造のLiCoO2が採用されるに至ってい
る。LiCoO2は、合成が容易でかつ取り扱いも比較
的容易であることに加え、充放電サイクル特性において
優れることから、LiCoO2を正極活物質に使用する
二次電池が主流となっている。At present, as a positive electrode active material of a lithium secondary battery, LiCoO 2 having an ordered layered rock salt structure has been adopted as a material capable of forming a 4V-class secondary battery. LiCoO 2 is easy to synthesize and relatively easy to handle, and is excellent in charge / discharge cycle characteristics. Therefore, a secondary battery using LiCoO 2 as a positive electrode active material is mainly used.
【0004】ところが、コバルトは資源量として少な
く、LiCoO2を正極活物質に使用した二次電池で
は、自動車用電池をにらんだ将来の量産化、大型化に対
応しにくく、また価格的にも極めて高価なものにならざ
るを得ない。そこでコバルトに代えて、比較的資源とし
て豊富でありかつ安価なマンガンを構成元素として含
む、リチウムマンガン複合酸化物を正極活物質に採用す
る試みがされている。[0004] However, cobalt is a scarce resource, and a secondary battery using LiCoO 2 as a positive electrode active material is difficult to cope with future mass production and size enlargement of automobile batteries, and also in terms of price. It must be very expensive. Therefore, instead of cobalt, an attempt has been made to employ a lithium manganese composite oxide containing manganese, which is relatively abundant and inexpensive as a constituent element, as a positive electrode active material.
【0005】正極活物質に用いることにより4V級のリ
チウム二次電池を構成することのできるリチウムマンガ
ン複合酸化物は、規則配列層状岩塩構造LiMnO2、
ジグザグ層状構造LiMnO2、スピネル構造LiMn2
O4のものが知られている。スピネル構造LiMn2O4
は、これらの中では比較的結晶構造が安定しており、理
論容量は小さいものの可逆的に吸蔵・放出できるリチウ
ム量が多く、リチウム二次電池を構成した場合に、上記
LiCoO2を用いたものとほぼ同等の放電容量が得ら
れることから、有力な次期リチウム二次電池用正極活物
質となり得る。[0005] A lithium manganese composite oxide which can constitute a 4V-class lithium secondary battery by being used as a positive electrode active material is composed of an ordered layered rock salt structure LiMnO 2 ,
Zigzag layered structure LiMnO 2 , spinel structure LiMn 2
Those of O 4 is known. Spinel structure LiMn 2 O 4
Among them, the crystal structure is relatively stable, and although the theoretical capacity is small, the amount of lithium that can be inserted and released reversibly is large, and when a lithium secondary battery is constructed, the above LiCoO 2 is used. Since the same discharge capacity as that described above can be obtained, it can be a promising positive electrode active material for the next lithium secondary battery.
【0006】従来、スピネル構造LiMn2O4の製造方
法としては、以下に掲げる固相反応によるものがあっ
た。 (1)Mn2O3またはMnO2とLi2CO3とを、M
n:Liがモル比で2:1となるように混合し、この混
合物を空気中において650℃で6時間ないしは850
℃で14時間焼成する方法(特開昭63−187569
号公報) (2)γ−MnOOHにリチウム塩を加え800℃に加
熱する方法(特開平3−4445号公報) (3)マンガン酸化物(MnO2、Mn2O3、Mn
3O4)とLiNO3との混合物を、空気中において80
0℃で焼成する方法(特開平3−67464号公報) (4)MnO2とLiNO3とを、Mn:Liがモル比で
2.2:1.0〜1.8:1.0となるように混合し、
この混合物を空気中において800℃以上1000℃以
下の温度範囲で焼成する方法(特開平3−127453
号公報) (5)LiNO3あるいはLiOHとMnO2とを混合
し、この混合物を260℃で保持した後、400〜50
0℃の温度で焼成し、再度600〜700℃の温度で焼
成する方法(特開平7−245106号公報)等であ
る。Hitherto, as a method for producing a spinel-structured LiMn 2 O 4 , there has been a solid-state reaction described below. (1) Mn 2 O 3 or MnO 2 and Li 2 CO 3
n: Li is mixed at a molar ratio of 2: 1 and the mixture is heated at 650 ° C. in air for 6 hours to 850 ° C.
Baking at 14 ° C. for 14 hours (JP-A-63-187569).
(2) A method of adding a lithium salt to γ-MnOOH and heating to 800 ° C. (JP-A-3-4445) (3) Manganese oxide (MnO 2 , Mn 2 O 3 , Mn)
The mixture of 3 O 4 ) and LiNO 3 is
(4) MnO 2 and LiNO 3 in a molar ratio of Mn: Li of 2.2: 1.0 to 1.8: 1.0. And mix
A method in which this mixture is fired in air at a temperature in the range of 800 ° C. to 1000 ° C. (JP-A-3-127453).
(5) LiNO 3 or LiOH and MnO 2 are mixed and the mixture is kept at 260 ° C.
A method of firing at a temperature of 0 ° C. and firing at a temperature of 600 to 700 ° C. again (JP-A-7-245106).
【0007】[0007]
【発明が解決しようとする課題】上記従来の製造方法で
は、結晶性の高いスピネル構造リチウムマンガン複合酸
化物を得るために、焼成する雰囲気を調整し、この調整
された雰囲気中で500℃以上もの高温度による焼成を
行っている。そのため大きなエネルギーを必要とし、製
造コスト自体も高くなるという問題があった。また、固
相反応による場合は、出発原料となる物質の混合比、つ
まりいわゆる仕込み段階での各構成元素の組成比を最終
生成物の組成比に整合させる必要があり、かつ、混合自
体も充分均一に行わなければならず、煩雑な工程になら
ざるを得ないという問題もあった。In the above-mentioned conventional production method, the firing atmosphere is adjusted in order to obtain a highly crystalline spinel-structured lithium manganese composite oxide, and the temperature of 500 ° C. or more is adjusted in this adjusted atmosphere. Baking at high temperature is performed. Therefore, there is a problem that a large amount of energy is required and the manufacturing cost itself is increased. In the case of the solid-phase reaction, it is necessary to match the mixing ratio of the starting materials, that is, the composition ratio of each constituent element in the so-called preparation stage, with the composition ratio of the final product, and the mixing itself is sufficient. There was also a problem that the process had to be performed uniformly and a complicated process had to be performed.
【0008】スピネル構造リチウムマンガン複合酸化物
は、正極活物質として用いる場合、組成式LiMn2O4
で表されるものばかりではない。リチウム二次電池のサ
イクル特性等を改善するために、結晶中のLiサイトあ
るいはMnサイトの一部を他元素で置換し、例えば、組
成式Li1-zAzMn2-yMeyO2で表されるリチウム複
合酸化物を、正極活物質として使用する場合もある。こ
のような他元素で置換したスピネル構造リチウムマンガ
ン複合酸化物を製造しようとする場合、原料物質の均一
な混合はより一層難しく、上記従来の固相反応による方
法では、結晶物全体における置換割合の均一性にも問題
を残し、従来法によるリチウムマンガン複合酸化物で
は、良好な充放電特性を有するリチウム二次電池を構成
できなかった。When the spinel-structured lithium manganese composite oxide is used as a positive electrode active material, the composition formula is LiMn 2 O 4
Not only those represented by. In order to improve the cycle characteristics of the lithium secondary battery, a portion of the Li site or Mn sites in the crystal was substituted by another element, for example, the composition formula Li 1-z A z Mn 2 -y Me y O 2 May be used as the positive electrode active material. When attempting to produce such a spinel-structured lithium manganese composite oxide substituted with another element, uniform mixing of the raw materials is even more difficult, and the above-described conventional solid-phase reaction method has a problem in that the substitution ratio of the entire crystal is reduced. Even with the problem of uniformity, the lithium manganese composite oxide according to the conventional method cannot form a lithium secondary battery having good charge / discharge characteristics.
【0009】本発明は、従来からの製造方法が抱える上
記問題を解決すべくなされたものであり、リチウム二次
電池用正極活物質となり得るスピネル構造リチウムマン
ガン複合酸化物の製造方法であって、結晶組成の均一性
に優れたリチウムマンガン複合酸化物を、簡便かつ低コ
ストに製造できる製造方法を提供することを目的とす
る。The present invention has been made in order to solve the above-mentioned problems of the conventional production method, and is a method for producing a lithium manganese composite oxide having a spinel structure which can be used as a positive electrode active material for a lithium secondary battery, An object of the present invention is to provide a production method capable of producing a lithium manganese composite oxide having excellent crystal composition uniformity easily and at low cost.
【0010】[0010]
【課題を解決するための手段】本発明のリチウム二次電
池正極活物質用リチウムマンガン複合酸化物の製造方法
は、Me(NO3)m(MeはMn、Ni、Co、Cr、
Fe、Al、Tiから選ばれる1種以上であってすくな
くともMnを含む、mはMeの価数に応じた値)を水に
溶解させた硝酸塩水溶液と、AOH(Aはアルカリ金属
から選ばれる1種以上であって少なくともLiを含む)
をH2O2水溶液に溶解させた水酸化物H 2O2水溶液とを
混合させて混合溶液とし、該混合溶液中に組成式AxM
eO2・nH2O(0<x≦1、0.1≦n≦1)で表さ
れる層状岩塩構造の複合酸化物前駆体を析出させる析出
工程と、析出後の前記混合溶液中で前記複合酸化物前駆
体を熟成させ、組成式AMe2O4で表されるスピネル構
造のリチウムマンガン複合酸化物を得る熟成工程とを含
んでなることを特徴とする。The lithium secondary battery of the present invention
Of Lithium-Manganese Composite Oxide for Pond Positive Electrode Active Material
Is Me (NOThree)m(Me is Mn, Ni, Co, Cr,
At least one selected from the group consisting of Fe, Al, and Ti
Containing at least Mn, m is the value corresponding to the valence of Me)
A dissolved nitrate solution and AOH (A is an alkali metal
At least one selected from the group consisting of at least Li)
To HTwoOTwoHydroxide H dissolved in aqueous solution TwoOTwoWith the aqueous solution
The mixture was mixed to form a mixed solution, and the composition formula A was added to the mixed solution.xM
eOTwo・ NHTwoO (0 <x ≦ 1, 0.1 ≦ n ≦ 1)
To deposit complex oxide precursor with layered rock salt structure
And the mixed oxide precursor in the mixed solution after deposition.
Aging body, formula AMeTwoOFourSpinel structure represented by
Aging step to obtain a lithium manganese composite oxide
It is characterized by becoming.
【0011】つまり本発明のリチウムマンガン複合酸化
物の製造方法は、スピネル構造のリチウムマンガン複合
酸化物の製造方法であって、マンガン源あるいはマンガ
ンおよびマンガンサイトを置換可能な他元素源となる硝
酸塩水溶液と、リチウム源またはリチウムおよびリチウ
ムサイトを置換可能なアルカリ金属元素源となる水酸化
物のH2O2水溶液とを混合し、溶液反応によって、層状
岩塩構造の複合酸化物前駆体を析出させ、この後、析出
した前駆体を比較的低温度中に保持して熟成させ、結晶
構造を層状岩塩構造からスピネル構造へ転移させるとい
うものである。That is, the method for producing a lithium manganese composite oxide according to the present invention is a method for producing a lithium manganese composite oxide having a spinel structure, wherein a nitrate aqueous solution serving as a manganese source or another element source capable of replacing manganese and manganese sites is provided. And an aqueous H 2 O 2 solution of a hydroxide serving as a lithium source or a source of an alkali metal element capable of replacing lithium and a lithium site, and by a solution reaction, a composite oxide precursor having a layered rock salt structure is precipitated, Thereafter, the deposited precursor is kept at a relatively low temperature and aged, and the crystal structure is changed from a layered rock salt structure to a spinel structure.
【0012】本発明のリチウムマンガン複合酸化物の製
造方法は、従来法の固相反応による方法と異なり、溶液
反応により前駆体を合成することで、原料物質の充分な
混合が確保され、最終生成物であるスピネル構造リチウ
ムマンガン複合酸化物は、生成物全体の組成の均一性に
優れたものとなる。また、熟成工程は、従来法の焼成と
は異なる比較的低温度の処理であるため、高温加熱をす
る場合ほどのエネルギーを必要とせず、燃費の小さいひ
いては製造コストの安い製造方法となる。さらにまた、
熟成工程は原料溶液を混合した混合溶液中での転移現象
を利用するため、原料溶液の混合比つまり仕込み段階で
のマンガンおよびリチウムの組成比の変化が、最終生成
物であるスピネル構造リチウムマンガン複合酸化物の組
成比に与える影響は小さい。したがって原料溶液の混合
に多大な注意を払う必要がない点で、本発明のリチウム
マンガン複合酸化物の製造方法は、簡便な製造方法とな
る。The method for producing a lithium-manganese composite oxide according to the present invention is different from the conventional method using a solid-phase reaction, in which a precursor is synthesized by a solution reaction, whereby sufficient mixing of the raw materials is ensured, and The spinel-structured lithium manganese composite oxide, which is a product, has excellent composition uniformity throughout the product. Further, the aging step is a relatively low-temperature treatment different from the conventional calcination, so that it does not require as much energy as heating at a high temperature, and has a low fuel consumption and a low production cost. Furthermore,
Since the aging process utilizes the transition phenomenon in the mixed solution of the raw material solutions, the change of the mixing ratio of the raw material solutions, that is, the change of the composition ratio of manganese and lithium in the charging stage, is caused by the spinel structure lithium manganese composite as the final product. The effect on the composition ratio of the oxide is small. Therefore, the method for producing a lithium manganese composite oxide according to the present invention is a simple production method because it is not necessary to pay great attention to mixing of the raw material solutions.
【0013】[0013]
【発明の実施の形態】以下に本発明のリチウム二次電池
正極活物質用リチウムマンガン複合酸化物の製造方法に
ついて、製造対象となり得るリチウムマンガン複合酸化
物、最初に行われる析出工程、続いて行われる熟成工程
の順に説明し、その後に、製造されたリチウムマンガン
複合酸化物の利用形態であるリチウム二次電池について
説明する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, a method for producing a lithium manganese composite oxide for a positive electrode active material of a lithium secondary battery according to the present invention will be described. The aging process will be described in the following order, and thereafter, a lithium secondary battery which is a use form of the manufactured lithium manganese composite oxide will be described.
【0014】〈製造対象となるリチウムマンガン複合酸
化物〉本発明のリチウム二次電池正極活物質用リチウム
マンガン複合酸化物の製造方法が製造の対象とするリチ
ウムマンガン複合酸化物は、スピネル構造のリチウムマ
ンガン複合酸化物である。対象となるリチウムマンガン
複合酸化物は、組成式LiMn2O4で表される化学量論
組成のものに限定されない。結晶構造の安定化に帰因さ
れるサイクル特性の向上、保存特性の向上等の目的で、
Mnサイトの一部を他元素の原子Me'で置換させた組
成式LiMn2-yMe'yO4で表されるもの、あるいは、
Liサイトの一部を他のアルカリ金属元素の原子A'で
置換させた組成式Li1-zA'zMn2O4で表されるもの
も含まれる。さらに、MnサイトおよびLiサイトの両
者の一部を他の元素の原子で置換した、組成式Li1-z
A' zMn2-yMe'yO4で表されるものも製造対象に含ま
れる。<Lithium manganese composite acid to be produced
> Lithium for the positive electrode active material of the lithium secondary battery of the present invention
Manufactured by the manganese composite oxide manufacturing method
Manganese composite oxide is a spinel-structured lithium
Ngan composite oxide. Target lithium manganese
The composite oxide has a composition formula of LiMnTwoOFourStoichiometry expressed by
It is not limited to the composition. Attributed to stabilization of crystal structure
Cycle characteristics, storage characteristics, etc.
A group in which a part of the Mn site is replaced by an atom Me ′ of another element
Formula LiMn2-yMe 'yOFourRepresented by, or
Part of the Li site is replaced with another alkali metal atom A '
Substituted composition formula Li1-zA 'zMnTwoOFourRepresented by
Is also included. Further, both the Mn site and the Li site
The composition formula Li in which part of the formula is replaced with atoms of another element1-z
A ' zMn2-yMe 'yOFourIncluded in manufacturing targets
It is.
【0015】Mnサイトの一部を他元素で置換する場合
は、その置換割合つまり組成式におけるyの値が、0<
y≦0.5となるもの製造するのが望ましい。この理由
は、2価が一部安定なMe'の置換割合が0.5を超え
ると、Mnが4価となって充放電可能なMn3+が存在し
なくなり、容量が激減するからである。また、Liサイ
トの一部を他のアルカリ金属原子で置換する場合は、そ
の置換割合つまり組成式中のzの値は、0<z≦0.3
とするのが望ましい。この理由は、これ以上置換すると
容量が1/2以下となるからである。When a part of the Mn site is substituted with another element, the substitution ratio, that is, the value of y in the composition formula is 0 <
It is desirable to manufacture those satisfying y ≦ 0.5. The reason for this is that, when the substitution ratio of Me ′, which is partially stable in divalent, exceeds 0.5, Mn becomes tetravalent and there is no Mn 3+ that can be charged and discharged, and the capacity is drastically reduced. . When a part of the Li site is substituted with another alkali metal atom, the substitution ratio, that is, the value of z in the composition formula, is 0 <z ≦ 0.3.
It is desirable that The reason for this is that the capacity will be reduced to 置換 or less if replaced further.
【0016】正極活物質として使用する場合、Mnサイ
トを置換させることのできる他の原子Me'には、N
i、Co、Cr、Fe、Al、Tiが挙げられる。これ
らはいずれも、3価で安定な原子であり、層状構造を安
定化させるという役割を果たす。これらの中でも、M
e'にNiを用いるのがより望ましい。Niは、3価の
イオン半径がMn3+とほぼ等しいため、結晶にほとんど
歪みを生じないからである。また、Liサイトを置換さ
せることのできるアルカリ金属A'には、Na、K、P
b、Csが挙げられる。これらのアルカリ金属は、充放
電に関係なく層間に存在し、常に層間のスペースを保持
するという役割を果たす。これらの中でも、A'にKを
用いるのがより望ましい。Kは、イオン半径がLiの約
2倍の大きさであり、かつ安価だからである。When used as a positive electrode active material, other atoms Me ′ capable of substituting Mn sites include N
i, Co, Cr, Fe, Al, and Ti. These are all trivalent and stable atoms and play a role in stabilizing the layered structure. Among these, M
It is more desirable to use Ni for e ′. This is because Ni has almost no distortion in the crystal because the trivalent ionic radius is substantially equal to Mn 3+ . The alkali metal A ′ capable of substituting the Li site includes Na, K, P
b and Cs. These alkali metals exist between the layers irrespective of charge and discharge, and play a role of always maintaining the space between the layers. Among these, it is more desirable to use K for A ′. This is because K has an ionic radius about twice as large as that of Li and is inexpensive.
【0017】〈析出工程〉本製造方法において最初に行
われる析出工程は、Me(NO3)m(MeはMn、N
i、Co、Cr、Fe、Al、Tiから選ばれる1種以
上であってすくなくともMnを含む、mはMeの価数に
応じた値)を水に溶解させた硝酸塩水溶液と、AOH
(Aはアルカリ金属から選ばれる1種以上であって少な
くともLiを含む)をH2O2水溶液に溶解させた水酸化
物H2O2水溶液とを混合させて混合溶液とし、この混合
溶液中に組成式AxMeO2・nH2O(0<x≦1、
0.1≦n≦1)で表される層状岩塩構造の複合酸化物
前駆体を析出させるものである。<Precipitation Step> The first precipitation step performed in the present manufacturing method is Me (NO 3 ) m (Me is Mn, N
a nitrate aqueous solution in which at least one selected from i, Co, Cr, Fe, Al and Ti and containing at least Mn, m is a value corresponding to the valency of Me) in water;
(A is at least one selected from alkali metals and contains at least Li) is mixed with an aqueous solution of hydroxide H 2 O 2 in which an aqueous solution of H 2 O 2 is dissolved to form a mixed solution. The composition formula A x MeO 2 .nH 2 O (0 <x ≦ 1,
This is to precipitate a composite oxide precursor having a layered rock salt structure represented by 0.1 ≦ n ≦ 1).
【0018】Me(NO3)mは、Mnサイトを他元素M
e'(Ni、Co、Cr、Fe、Al、Tiから選ばれ
る1種以上)の原子で置換させない場合、Mn(N
O3)2を用いればよい。Mnサイトの一部を他元素M
e'の原子で置換させる場合は、Mn(NO3)2とMe'
(NO3)m'(m'はMe'の価数に応じた値)とを、M
nとMe'とのモル比が、2−y:y(yは上記置換割
合)となるように混合し、水に溶解させればよい。ま
た、Me(NO3)m水溶液の濃度は、0.1〜1Mであ
るのが望ましい。これは、0.1M未満の場合は析出量
が少なく、また、1Mを超える場合には、酸素の発生が
多くなり危険を伴う可能性があるからである。Me (NO 3 ) m changes the Mn site to another element M
When not substituted with an atom of e ′ (one or more selected from Ni, Co, Cr, Fe, Al, and Ti), Mn (N
O 3 ) 2 may be used. Part of the Mn site is replaced with another element M
When substituting with the atom of e ′, Mn (NO 3 ) 2 and Me ′
(NO 3 ) m ′ (m ′ is a value corresponding to the valence of Me ′) and M
What is necessary is just to mix so that the molar ratio of n and Me 'is 2-y: y (y is the above-mentioned substitution ratio), and to dissolve in water. The concentration of the aqueous solution of Me (NO 3 ) m is desirably 0.1 to 1M. This is because when the concentration is less than 0.1 M, the amount of precipitation is small, and when it exceeds 1 M, generation of oxygen increases, which may be dangerous.
【0019】AOHは、Liサイトを他のアルカリ金属
元素A'(Liを除くアルカリ金属から選ばれる1種以
上)の原子で置換させない場合は、LiOHを用いれば
よい。Liサイトの一部を他のアルカリ金属元素A'の
原子で置換させる場合は、LiOHとA'OHとを、L
iとA'とのモル比が1−z:z(zは上記置換割合)
となるように、混合して溶解させればよい。AOH may be used when the Li site is not replaced by an atom of another alkali metal element A '(at least one selected from alkali metals except Li). When a part of the Li site is replaced with an atom of another alkali metal element A ′, LiOH and A′OH are replaced by L
The molar ratio between i and A 'is 1-z: z (z is the above substitution ratio)
What is necessary is just to mix and melt | dissolve so that it may become.
【0020】AOHを溶解させる溶媒としてH2O2水溶
液を用いるのは、水溶性のMn2+を不溶性のMn3+に酸
化させるためである。このH2O2水溶液の濃度は、反応
の安全性を考え、1〜10wt%とすることが望まし
い。またH2O2水溶液に溶解させるAOHの濃度は、均
一な反応を行うために、0.2〜5Mであることが望ま
しい。The reason for using an aqueous solution of H 2 O 2 as a solvent for dissolving AOH is to oxidize water-soluble Mn 2+ to insoluble Mn 3+ . The concentration of the H 2 O 2 aqueous solution is desirably 1 to 10 wt% in consideration of the safety of the reaction. The concentration of AOH dissolved in the aqueous solution of H 2 O 2 is desirably 0.2 to 5 M in order to perform a uniform reaction.
【0021】析出工程におけるMe(NO3)m硝酸塩水
溶液とAOH水酸化物H2O2水溶液との混合割合は、析
出させる複合酸化物前駆体の組成式AxMeO2・nH2
Oにおけるxの値(Aの存在割合)応じて変更させれば
よい。0<x≦1の範囲のものを析出させようとする場
合には、Me:Aがモル比で1:3〜1:10の割合と
なるように混合させる。The mixing ratio of the aqueous solution of Me (NO 3 ) m nitrate and the aqueous solution of AOH hydroxide H 2 O 2 in the precipitation step is determined by the composition formula A x MeO 2 .nH 2 of the composite oxide precursor to be deposited.
What is necessary is just to change according to the value of x in O (existence ratio of A). When it is desired to precipitate those in the range of 0 <x ≦ 1, Me: A is mixed at a molar ratio of 1: 3 to 1:10.
【0022】本発明の製造方法では、析出工程で析出し
た複合酸化物前駆体の組成式AxMeO2・nH2O中の
xの値によらず、最終生成物であるスピネル構造のリチ
ウムマンガン複合酸化物は組成式AMe2O4で表される
ものとなる。したがって、Me(NO3)m硝酸塩水溶液
とAOH水酸化物H2O2水溶液との混合割合が最終生成
物の組成に影響を及ぼさないことから、両溶液の混合比
に多大な注意を払う必要がなく、その点で簡便な製造方
法といえる。ただし、後の熟成工程、水洗方法、乾燥工
程等に配慮すれば、前駆体であるAxMeO2・nH2O
のxの値は0.2≦x≦0.7の範囲とするのが実用的
であり、そのためには、Me(NO3)m硝酸塩水溶液と
AOH水酸化物H2O2水溶液との混合割合は、Me:A
がモル比で1:3〜1:5の割合となるように混合させ
るのが望ましい。In the production method of the present invention, regardless of the value of x in the composition formula A x MeO 2 .nH 2 O of the composite oxide precursor deposited in the precipitation step, lithium manganese having a spinel structure, which is a final product, The composite oxide is represented by the composition formula AMe 2 O 4 . Therefore, since the mixing ratio of the aqueous solution of Me (NO 3 ) m nitrate and the aqueous solution of AOH hydroxide H 2 O 2 does not affect the composition of the final product, great care must be paid to the mixing ratio of both solutions. Therefore, it can be said that this is a simple manufacturing method. However, if consideration is given to the subsequent aging step, washing method, drying step, etc., the precursor A x MeO 2 .nH 2 O
It is practical to set the value of x in the range of 0.2 ≦ x ≦ 0.7. For this purpose, a mixture of an aqueous solution of Me (NO 3 ) m nitrate and an aqueous solution of AOH hydroxide H 2 O 2 is used. The ratio is Me: A
Are desirably mixed such that the molar ratio is 1: 3 to 1: 5.
【0023】ちなみに、Mn(NO3)2を溶解させた水
溶液とLiOHを溶解させたH2O2水溶液とを混合させ
て析出反応を起こさせれば、析出する複合酸化物前駆体
は組成式LixMnO2・nH2Oで表されるものとな
る。同様に、Mn(NO3)2とMe'(NO3)m'とを溶
解させた水溶液とLiOHを溶解させたH2O2水溶液と
を混合させれば、複合酸化物前駆体は組成式LixMn
1-y/2Me'y/2O2・nH2Oで表されるものとなり、ま
た、Mn(NO3)2を溶解させた水溶液とLiOHと
A'OHとを溶解させたH2O2水溶液とを混合させれ
ば、複合酸化物前駆体は組成式(Li1-zA'z)xMnO
2・nH2Oで表されるものとなり、さらにまた、Mn
(NO3)2とMe'(NO3)m'とを溶解させた水溶液と
LiOHとA'OHとを溶解させたH2O2水溶液とを混
合させれば、複合酸化物前駆体は組成式(Li
1-zA'z)xMn1-y/2Me'y/2O2・nH2Oで表される
ものとなる。By the way, if an aqueous solution in which Mn (NO 3 ) 2 is dissolved and an aqueous solution of H 2 O 2 in which LiOH is mixed to cause a precipitation reaction, the composite oxide precursor to be deposited has a composition formula of Li x MnO 2 · nH 2 O. Similarly, if an aqueous solution in which Mn (NO 3 ) 2 and Me ′ (NO 3 ) m ′ are dissolved and an aqueous solution of H 2 O 2 in which LiOH is dissolved, the composite oxide precursor has a composition formula Li x Mn
1-y / 2 Me'y / 2 O 2 · nH 2 O, and an aqueous solution in which Mn (NO 3 ) 2 is dissolved and an H 2 O in which LiOH and A'OH are dissolved 2 aqueous solution, the composite oxide precursor has the composition formula (Li 1-z A ′ z ) x MnO
2 · nH 2 O, and Mn
By mixing an aqueous solution in which (NO 3 ) 2 and Me ′ (NO 3 ) m ′ are dissolved and an aqueous solution of H 2 O 2 in which LiOH and A′OH are dissolved, the composite oxide precursor has a composition The formula (Li
1-z A ′ z ) x Mn 1−y / 2 Me ′ y / 2 O 2 .nH 2 O
【0024】析出工程は、硝酸塩水溶液と水酸化物H2
O2水溶液とを均一に混合することによって行う。この
均一性を確保するために、両者の混合は攪拌しながら行
うことが望ましい。攪拌の方法は特に限定されるもので
はなく、通常の溶液を攪拌させる公知の方法に従えばよ
い。析出工程における反応温度は、発熱反応を伴うとい
う理由から、10〜30℃で行うのが望ましい。また、
析出工程における反応時間は、1〜30分間行えばよ
く、比較的迅速な工程となる。In the precipitation step, an aqueous nitrate solution and hydroxide H 2 are used.
This is performed by uniformly mixing with an O 2 aqueous solution. In order to ensure this uniformity, it is desirable to mix the two while stirring. The method of stirring is not particularly limited, and a known method of stirring a normal solution may be used. The reaction temperature in the precipitation step is desirably 10 to 30 ° C. because it involves an exothermic reaction. Also,
The reaction time in the precipitation step may be 1 to 30 minutes, which is a relatively quick step.
【0025】この析出工程によって析出した複合酸化物
前駆体は、組成式AxMeO2・nH 2O(0.1≦n≦
1)で表され、組成式から明らかなように水和水を含ん
でおり、結晶性は低い。この水和水の割合つまり組成式
中のnの値は、析出における反応条件により異なるもの
となり、0.1≦n≦1の範囲で定かではない。nの値
がこの範囲のいかなる値であっても、後の熟成工程にお
いて除去され、最終生成物であるスピネル構造のリチウ
ムマンガン複合酸化物には水和水は存在しなくなる。ち
なみに、0.3MのMe(NO3)m水溶液と0.6Mの
AOHの3wt%H2O2水溶液とを混合させ、20℃の
温度下、5分間反応させた場合、nの値は0.6程度と
なる。The composite oxide deposited by this precipitation step
The precursor has the composition formula AxMeOTwo・ NH TwoO (0.1 ≦ n ≦
1) containing water of hydration as is clear from the composition formula
And the crystallinity is low. The ratio of this hydration water, that is, the composition formula
The value of n in the table depends on the reaction conditions in the precipitation
It is not clear in the range of 0.1 ≦ n ≦ 1. the value of n
Is any value in this range,
Removed, and the final product, lithium, with spinel structure
Water of hydration no longer exists in the manganese composite oxide. Chi
By the way, 0.3M Me (NOThree)mAqueous solution and 0.6M
3 wt% H of AOHTwoOTwoMixed with an aqueous solution at 20 ° C
When reacted at a temperature for 5 minutes, the value of n is about 0.6
Become.
【0026】〈熟成工程〉本発明の製造方法における熟
成工程は、組成式AxMeO2・nH2O(0<x≦1、
0.1≦n≦1)で表される層状岩塩構造の複合酸化物
前駆体を、この前駆を析出させた後の混合溶液中で、所
定範囲の温度に保持したまま熟成(いわゆるエージン
グ)させ、組成式AMe2O4で表されるスピネル構造の
リチウムマンガン複合酸化物に転移させる工程である。<Aging Step> The aging step in the production method of the present invention comprises a composition formula A x MeO 2 .nH 2 O (0 <x ≦ 1,
The complex oxide precursor having a layered rock salt structure represented by 0.1 ≦ n ≦ 1) is aged (so-called aging) in a mixed solution after the precipitation of the precursor while maintaining the temperature within a predetermined range. This is a step of transferring to a lithium manganese composite oxide having a spinel structure represented by a composition formula AMe 2 O 4 .
【0027】保持する温度つまり熟成温度において好適
となる温度範囲は、Mnサイトの一部をを他元素で置換
するか否かによって異なるものとなる。Mnサイトを置
換させないものを製造する場合、つまり組成式LiMn
2O4あるいはLi1-zA'zMn2O4で表されるリチウム
マンガン複合酸化物を製造する場合は、50℃を超え2
00℃未満の温度に保持して熟成させるのが望ましい。
また、Mnサイトの一部を置換させたものを製造する場
合、つまりLiMn2-yMe'yO4あるいはLi 1-zA'z
Mn2-yMe'yO4で表されるリチウムマンガン複合酸化
物を製造する場合は、50℃を超え300℃未満の温度
に保持して熟成させるのが望ましい。Suitable at holding temperature, that is, aging temperature
Temperature range, part of the Mn site is replaced with another element
It depends on whether or not to do so. Place Mn site
In the case of manufacturing a product not to be exchanged, that is, the composition formula LiMn
TwoOFourOr Li1-zA 'zMnTwoOFourLithium represented by
When manufacturing a manganese composite oxide, use
It is desirable to keep the temperature below 00 ° C. for aging.
In addition, when manufacturing a product in which a part of the Mn site is substituted,
In other words, LiMn2-yMe 'yOFourOr Li 1-zA 'z
Mn2-yMe 'yOFourLithium manganese composite oxidation represented by
In the case of manufacturing products, the temperature is more than 50 ℃ and less than 300 ℃
It is desirable to keep and aged.
【0028】熟成温度が50℃以下の場合は、結晶構造
が変化しない未反応物、言い換えれば前駆体のままの相
が残存する。逆に200℃あるいは300℃以上の場合
は、スピネル構造のもの以外に、水和水を含まない規則
層状岩塩構造のものが転移により副生し、やはり2つの
相が共存するものとなる。このような不純物相となるス
ピネル構造以外の相の存在は、このリチウムマンガン複
合酸化物を用いてリチウム二次電池を構成させた場合、
電池の充放電サイクル特性を悪化させる原因となる。し
たがって、スピネル構造単一相のリチウムマンガン複合
酸化物を製造させるという意味において、上記好適温度
範囲で熟成することが望ましい形態となる。なお、Mn
サイトを置換するか否かで上限の温度が変化するのは、
2価が安定な置換原子の存在によりMn4+が出現し、ス
ピネルが安定相になるためであると考えられる。When the aging temperature is 50 ° C. or lower, an unreacted substance whose crystal structure does not change, in other words, a phase as a precursor remains. On the other hand, when the temperature is 200 ° C. or 300 ° C. or higher, in addition to the spinel structure, a regular layered rock salt structure not containing hydration water is by-produced by the transformation, and the two phases also coexist. The existence of such a phase other than the spinel structure serving as the impurity phase is caused when a lithium secondary battery is formed using this lithium manganese composite oxide.
It causes deterioration of the charge / discharge cycle characteristics of the battery. Therefore, in order to produce a single-phase lithium manganese composite oxide having a spinel structure, it is desirable that the ripening be performed in the above-mentioned preferable temperature range. Note that Mn
The maximum temperature changes depending on whether the site is replaced or not.
It is considered that Mn 4+ appears due to the presence of a divalent stable substituent atom, and spinel becomes a stable phase.
【0029】より純粋なスピネル構造単一相のものを製
造しようとする場合、上記好適熟成温度範囲の上限また
は下限の温度付近は避けるのがよく、熟成温度の範囲
を、Mnサイトを置換させないものを製造する場合は、
70℃以上150℃以下とするのがより望ましく、Mn
サイトの一部を他元素の原子で置換させたものを製造す
る場合は、70℃以上200℃以下とするのがより望ま
しい。When a single phase having a more pure spinel structure is to be produced, it is preferable to avoid the vicinity of the upper limit or the lower limit of the above-mentioned preferable ripening temperature range. If you manufacture
It is more preferable that the temperature is 70 ° C. or more and 150 ° C. or less.
In the case of manufacturing a product in which a part of a site is replaced with an atom of another element, it is more preferable that the temperature be 70 ° C or more and 200 ° C or less.
【0030】熟成させる時間は、熟成温度等の条件によ
って異なるものとなるが、熟成反応が完全に終了し得る
時間であればよく、通常、6時間以上行えばよい。反応
終了後も熟成を行うことは、製造工程全体を引き延ばす
ことにつながるため、できるだけ短い時間とするのが望
ましい。熟成工程は、例えば、テフロンで内張りされた
オートクレーブに、析出工程で得られた溶液を入れ、1
50℃で12時間保持し、その後60℃以下まで冷却し
てから取り出すようにして行うことができる。ただし、
熟成温度が100℃付近あるいは100℃以上となると
混合溶液自体の蒸発が問題となるため、この溶液の蒸発
を防止すべく、100℃以下では還流器等によって、1
00℃以上となる場合はオートクレーブ容器等によって
行う必要がある。より簡便な装置で熟成工程を行うとい
った観点からすれば、熟成温度は60℃以上90℃以下
の範囲とするのが望ましい。The aging time varies depending on conditions such as the aging temperature and the like, but may be any time as long as the aging reaction can be completely completed, and is usually performed for 6 hours or more. Since aging after the completion of the reaction leads to elongation of the whole production process, it is desirable to shorten the time as much as possible. In the aging step, for example, the solution obtained in the precipitation step is placed in an autoclave lined with Teflon, and
The temperature can be kept at 50 ° C. for 12 hours, then cooled to 60 ° C. or less, and then taken out. However,
If the ripening temperature is around 100 ° C. or more than 100 ° C., evaporation of the mixed solution itself becomes a problem.
When the temperature is higher than 00 ° C., it is necessary to carry out in an autoclave container or the like. From the viewpoint of performing the ripening step with a simpler apparatus, the ripening temperature is desirably in the range of 60 ° C to 90 ° C.
【0031】上述したように行う熟成工程により、複合
酸化物前駆体は、層状岩塩構造から転移し、同時に含ま
れていた水和水は除去され、水和水を含まないスピネル
構造単一相のリチウムマンガン複合酸化物として生成さ
れる。ちなみに複合酸化物前駆体が組成式LixMnO2
・nH2Oで表されるものは組成式LiMn2O4で表さ
れるものとなり、同様に、LixMn1-y/2Me'y/2O2
・nH2Oで表されるものはLiMn2-yMe'yO4と、
また、(Li1-zA'z)xMnO2・nH2Oで表されるも
のはLi1-zA'zMn2O4と、さらにまた、(Li
1-zA'z)xMn1-y/2Me'y/2O2・nH2Oで表される
ものはLi1-zA'zMn2-yMe'yO4となる。生成され
たスピネル構造リチウムマンガン複合酸化物は、溶液中
から濾過することにより濾別し、水洗した後乾燥を行っ
て粉末状ものとする。なお、乾燥の方法は特に限定する
ものでなく、一般に行われているように、乾燥炉等に
て、50〜120℃の温度下、60〜180分間程度行
えばよい。By the aging step performed as described above, the composite oxide precursor is transformed from the layered rock salt structure, the water of hydration contained at the same time is removed, and the single phase of spinel structure containing no water of hydration is removed. Produced as lithium manganese composite oxide. Incidentally, the composite oxide precursor has a composition formula of Li x MnO 2
What is represented by nH 2 O is represented by the composition formula LiMn 2 O 4 , and similarly, Li x Mn 1-y / 2 Me ′ y / 2 O 2
The one represented by nH 2 O is LiMn 2-y Me ′ y O 4 ;
Further, those represented by (Li 1 -z A ' z ) x MnO 2 · nH 2 O are referred to as Li 1 -z A' z Mn 2 O 4 and further (Li
1-z A 'z) x Mn 1-y / 2 Me' y / 2 O 2 · nH those represented by 2 O becomes Li 1-z A 'z Mn 2-y Me' y O 4. The produced spinel-structured lithium manganese composite oxide is separated from the solution by filtration, washed with water, and then dried to form a powder. The drying method is not particularly limited, and may be performed in a drying furnace or the like at a temperature of 50 to 120 ° C. for about 60 to 180 minutes, as is generally performed.
【0032】〈リチウム二次電池〉本発明の製造方法で
得られたスピネル構造リチウムマンガン複合酸化物の利
用形態であるリチウム二次電池の実施形態について説明
する。一般にリチウム二次電池は、リチウムイオンを吸
蔵・放出する正極および負極と、この正極と負極との間
に挟装されるセパレータと、正極と負極の間をリチウム
イオンを移動させる非水電解液とから構成される。本実
施形態の二次電池もこの構成に従うため、以下の説明
は、これらの構成要素のそれぞれについて行うこととす
る。<Lithium Secondary Battery> An embodiment of a lithium secondary battery, which is an application of the spinel-structured lithium manganese composite oxide obtained by the production method of the present invention, will be described. Generally, a lithium secondary battery includes a positive electrode and a negative electrode that occlude and release lithium ions, a separator that is interposed between the positive electrode and the negative electrode, and a nonaqueous electrolyte that moves lithium ions between the positive electrode and the negative electrode. Consists of Since the secondary battery of the present embodiment also follows this configuration, the following description will be made for each of these components.
【0033】正極は、リチウムイオンを吸蔵・放出でき
る正極活物質に導電材および結着剤を混合し、必要に応
じ適当な溶媒を加えて、ペースト状の正極合材としたも
のを、アルミニウム等の金属箔製の集電体表面に塗布、
乾燥し、その後プレスによって活物質密度を高めること
によって形成する。本実施形態においては、正極活物質
は上記の製造方法で得られた組成式AMe 2O4で表され
るスピネル構造のリチウムマンガン複合酸化物を用い
る。Mnサイトの他元素の原子での置換割合、Liサイ
トの他のアルカリ金属原子での置換割合によって様々な
リチウムマンガン複合化合物が正極活物質となり得る。
本実施形態の二次電池では、これらのうち1種類のもの
を正極活物質として用いることも、また2種以上のもの
を混合して用いることもできる。さらに、上記リチウム
マンガン化合物と、既に公知となっている他の正極活物
質、例えば、LiCoO 2、LiNiO2等と混合して使
用するものであってもよい。The positive electrode can absorb and release lithium ions.
Mix the conductive material and binder with the positive electrode active material
An appropriate solvent was added to make a paste-like positive electrode mixture.
Is applied to the surface of a current collector made of metal foil such as aluminum,
Drying and then pressing to increase the active material density
Formed by In the present embodiment, the positive electrode active material
Is the composition formula AMe obtained by the above-mentioned production method. TwoOFourRepresented by
Using spinel-structured lithium manganese composite oxide
You. Substitution ratio of Mn site with other element atom, Li site
Can vary depending on the percentage of substitution with other alkali metal atoms.
A lithium manganese composite compound can be a positive electrode active material.
In the secondary battery of the present embodiment, one of these
Can be used as a positive electrode active material, or two or more
Can also be used as a mixture. In addition, the above lithium
Manganese compounds and other known positive electrode active materials
Quality, for example LiCoO Two, LiNiOTwoMixed with
May be used.
【0034】正極に用いる導電材は、正極活物質層の電
気伝導性を確保するためのものであり、カーボンブラッ
ク、アセチレンブラック、黒鉛等の炭素物質粉状体の1
種又は2種以上を混合したものを用いることができる。
結着剤は、活物質粒子を繋ぎ止める役割を果たすもの
で、ポリテトラフルオロエチレン、ポリフッ化ビニリデ
ン、フッ素ゴム等の含フッ素樹脂、ポリプロピレン、ポ
リエチレン等の熱可塑性樹脂を用いることができる。こ
れら活物質、導電材、結着剤を分散させる溶媒として
は、N−メチル−2−ピロリドン等の有機溶媒を用いる
ことができる。The conductive material used for the positive electrode is for ensuring the electric conductivity of the positive electrode active material layer, and is made of a carbon material powder such as carbon black, acetylene black, graphite or the like.
A species or a mixture of two or more species can be used.
The binder plays a role of binding the active material particles, and may be a fluororesin such as polytetrafluoroethylene, polyvinylidene fluoride, or fluororubber, or a thermoplastic resin such as polypropylene or polyethylene. As a solvent in which the active material, the conductive material, and the binder are dispersed, an organic solvent such as N-methyl-2-pyrrolidone can be used.
【0035】本実施形態での負極は、負極活物質である
金属リチウムを、一般の電池のそれと同様に、シート状
にして、あるいはシート状にしたものをニッケル、ステ
ンレス等の集電体網に圧着して形成する。負極活物質に
は金属リチウムに代え、リチウム合金またはリチウム化
合物をも用いることができる。また負極のもう一つの態
様として、負極活物質にリチウムイオンを吸蔵・放出で
きる炭素物質を用いて負極を構成させることもできる。
使用できる炭素物質としては、天然あるいは人造の黒
鉛、フェノール樹脂等の有機化合物焼成体、コークス等
の粉状体が挙げられる。この場合は、負極活物質に結着
剤を混合し、適当な溶媒を加えてペースト状にした負極
合材を、銅等の金属箔集電体の表面に塗布乾燥して形成
する。The negative electrode in the present embodiment is formed by sheeting metal lithium, which is the negative electrode active material, into a current collector network such as nickel or stainless steel in the same manner as that of a general battery. It is formed by pressing. As the negative electrode active material, a lithium alloy or a lithium compound can be used instead of metal lithium. As another embodiment of the negative electrode, the negative electrode can be formed using a carbon material capable of inserting and extracting lithium ions as the negative electrode active material.
Examples of the carbon substance that can be used include natural or artificial graphite, fired organic compounds such as phenolic resins, and powders such as coke. In this case, the binder is mixed with the negative electrode active material, and a suitable solvent is added thereto to form a paste-like negative electrode mixture on a surface of a metal foil current collector of copper or the like, followed by drying.
【0036】炭素物質を負極活物質とした場合、正極同
様、負極結着剤としてはポリフッ化ビニリデン等の含フ
ッ素樹脂等を、溶媒としてはN−メチル−2−ピロリド
ン等の有機溶媒を用いることができる。正極と負極の間
に挟装されるセパレータは、正極と負極とを隔離しつつ
電解液を保持してイオンを通過させるものであり、ポリ
エチレン、ポリプロピレン等の薄い微多孔膜を用いるこ
とができる。When the carbon material is used as the negative electrode active material, a fluorine-containing resin such as polyvinylidene fluoride or the like is used as the negative electrode binder and an organic solvent such as N-methyl-2-pyrrolidone is used as the solvent, similarly to the positive electrode. Can be. The separator sandwiched between the positive electrode and the negative electrode is for separating the positive electrode and the negative electrode and holding the electrolytic solution to allow the passage of ions, and a thin microporous film of polyethylene, polypropylene, or the like can be used.
【0037】非水電解液は、有機溶媒に電解質を溶解さ
せたもので、有機溶媒としては、非プロトン性有機溶
媒、例えばエチレンカーボネート、プロピレンカーボネ
ート、ジメチルカーボネート、ジエチルカーボネート、
γブチロラクトン、アセトニトリル、ジメトキシエタ
ン、テトラヒドロフラン、ジオキソラン、塩化メチレン
等の1種またはこれらの2種以上の混合液を用いること
ができる。また、溶解させる電解質としては、溶解させ
ることによりリチウムイオンを生じるLiI、LiCl
O4、LiAsF6、LiBF4、LiPF6等を用いるこ
とができる。なお非水電解液に代えて、固体電解質等を
用いることもできる。The non-aqueous electrolyte is obtained by dissolving an electrolyte in an organic solvent. Examples of the organic solvent include aprotic organic solvents such as ethylene carbonate, propylene carbonate, dimethyl carbonate, diethyl carbonate, and the like.
One kind of γ-butyrolactone, acetonitrile, dimethoxyethane, tetrahydrofuran, dioxolane, methylene chloride and the like, or a mixture of two or more kinds thereof can be used. As the electrolyte to be dissolved, LiI, LiCl which generates lithium ions when dissolved are used.
O 4 , LiAsF 6 , LiBF 4 , LiPF 6 and the like can be used. Note that a solid electrolyte or the like can be used instead of the non-aqueous electrolyte.
【0038】以上のものから構成される本実施形態のリ
チウム二次電池であるが、その形状はコイン型、積層
型、円筒型等の種々のものとすることができる。いずれ
の形状を採る場合であっても、正極および負極にセパレ
ータを挟装させ電極体とし、正極および負極から外部に
通ずる正極端子および負極端子までの間をそれぞれ導通
させるようにして、この電極体を非水電解液とともに電
池ケースに密閉して電池を完成させる。The lithium secondary battery of the present embodiment composed of the above-mentioned ones can have various shapes such as a coin type, a stacked type and a cylindrical type. In any case, a separator is sandwiched between the positive electrode and the negative electrode to form an electrode body, and the electrode body is made to conduct from the positive electrode and the negative electrode to the positive electrode terminal and the negative electrode terminal communicating with the outside, respectively. Together with the non-aqueous electrolyte in a battery case to complete the battery.
【0039】[0039]
【実施例】上記本発明の製造方法により、良好な正極活
物質用リチウムマンガン複合酸化物ができることを確認
すべく、種々の態様の方法でリチウムマンガン複合酸化
物を製造し、これらを評価した。以下に、実施例として
説明する。〈析出熟成法Aによるリチウムマンガン複合
酸化物〉Mn(NO3)2を溶解させた水溶液とLiOH
を溶解させたH2O2水溶液とを混合させて複合酸化物前
駆体を析出させ、この前駆体を種々の温度で熟成させて
製造した、Mnサイト、Liサイトのいずれもを置換さ
せていないリチウムマンガン複合酸化物である。なお、
本発明の製造方法である、析出工程と熟成工程とからな
る製造方法を、以下、「析出熟成法」ということにす
る。EXAMPLES In order to confirm that a good lithium manganese composite oxide for a positive electrode active material can be produced by the above production method of the present invention, lithium manganese composite oxides were produced by various methods and evaluated. Hereinafter, an embodiment will be described. <Lithium-manganese composite oxide by precipitation aging method A> An aqueous solution in which Mn (NO 3 ) 2 is dissolved and LiOH
Is mixed with an aqueous solution of H 2 O 2 in which is dissolved to precipitate a composite oxide precursor, and the precursor is aged at various temperatures. It is a lithium manganese composite oxide. In addition,
The production method comprising the precipitation step and the aging step, which is the production method of the present invention, is hereinafter referred to as “precipitation aging method”.
【0040】まず、0.3MのMn(NO3)2水溶液1
00mlに0.6MのLiOH/3wt%H2O2水溶液
200mlを混合させて混合溶液とし、スタラーピース
(攪拌装置)を用いて激しく攪拌させつつ5分間反応さ
せて、組成式Li0.6MnO2・0.5H2Oで表される
層状岩塩構造の複合酸化物前駆体を析出させた。次い
で、この前駆体を析出後の混合溶液ごとテフロンで内張
りした容器に入れ、室温および50℃〜200℃の範囲
の各種温度で、2日間かけて熟成させ、その後、濾別、
水洗、乾燥させて各種リチウムマンガン複合酸化物を得
た。そしてこれらを析出熟製法Aによるリチウムマンガ
ン複合酸化物とした。First, a 0.3 M Mn (NO 3 ) 2 aqueous solution 1
00ml in by mixing LiOH / 3wt% H 2 O 2 aqueous solution 200ml of 0.6M and the mixed solution, and reacted for 5 minutes while vigorously stirred with a Sutarapisu (stirrer), the compositional formula Li 0.6 MnO 2 · 0 A composite oxide precursor having a layered rock salt structure represented by 0.5H 2 O was precipitated. Next, this precursor was placed in a container lined with Teflon together with the mixed solution after deposition, aged at room temperature and various temperatures in the range of 50 ° C. to 200 ° C. for 2 days, and then separated by filtration.
After washing with water and drying, various lithium manganese composite oxides were obtained. And these were made into the lithium manganese composite oxide by the precipitation ripening manufacturing method A.
【0041】〈析出熟成法Bによるリチウムマンガン複
合酸化物〉Mn(NO3)2とNi(NO3)2を溶解させ
た水溶液とLiOHを溶解させたH2O2水溶液とを混合
させて複合酸化物前駆体を析出させ、この前駆体を種々
の温度で熟成させて製造した、Mnサイトの一部をNi
で置換させたリチウムマンガン複合酸化物である。<Lithium-manganese composite oxide by precipitation aging method B> An aqueous solution in which Mn (NO 3 ) 2 and Ni (NO 3 ) 2 are dissolved and an aqueous H 2 O 2 solution in which LiOH is dissolved are mixed to form a composite. An oxide precursor was precipitated, and this precursor was aged at various temperatures.
Is a lithium manganese composite oxide substituted with
【0042】まず、0.3MのMn(NO3)2水溶液と
0.3MのNi(NO3)2水溶液とをMn:Niがモル
比で19:1、18:2となるように混合した2つの水
溶液をそれぞれ100mlずつ調製した。それぞれの水
溶液に0.6MのLiOH/3wt%H2O2水溶液20
0mlを混合させて混合溶液とし、スタラーピースを用
いて激しく攪拌させつつ5分間反応させて、それぞれ組
成式Li0.6Mn0.95Ni0.05O2・0.4H2O、Li
0.5Mn0.9Ni0.1O2・0.5H2Oで表される2種の
層状岩塩構造の複合酸化物前駆体を析出させた。次い
で、これらの前駆体を析出後の混合溶液ごとテフロンで
内張りした容器に入れ、上記析出熟成法Aの場合と同
様、室温および50℃〜200℃の範囲の各種温度で、
2日間かけて熟成させ、その後、濾別、水洗、乾燥させ
て各種リチウムマンガン複合酸化物を得た。そしてこれ
らを析出熟成法Bによるリチウムマンガン複合酸化物と
した。First, a 0.3 M Mn (NO 3 ) 2 aqueous solution and a 0.3 M Ni (NO 3 ) 2 aqueous solution were mixed so that the molar ratio of Mn: Ni was 19: 1 and 18: 2. 100 ml of each of the two aqueous solutions was prepared. Each aqueous solution contains 0.6M LiOH / 3wt% H 2 O 2 aqueous solution 20
0 ml was mixed to form a mixed solution, and the mixture was reacted for 5 minutes with vigorous stirring using a stirrer piece to obtain a composition formula of Li 0.6 Mn 0.95 Ni 0.05 O 2 .0.4H 2 O, Li
Two types of composite oxide precursors having a layered rock salt structure represented by 0.5 Mn 0.9 Ni 0.1 O 2 · 0.5 H 2 O were deposited. Next, these precursors were placed in a container lined with Teflon together with the mixed solution after deposition, and, as in the case of the above-mentioned precipitation aging method A, at room temperature and at various temperatures in the range of 50 ° C to 200 ° C,
It was aged for 2 days, and then filtered, washed with water and dried to obtain various lithium manganese composite oxides. And these were made into the lithium manganese composite oxide by the precipitation aging method B.
【0043】〈析出熟成法Cによるリチウムマンガン複
合酸化物〉Mn(NO3)2とNi(NO3)2を溶解させ
た水溶液とLiOHとKOHとを溶解させたH2O2水溶
液とを混合させて複合酸化物前駆体を析出させ、この前
駆体を種々の温度で熟成させて製造した、Mnサイトの
一部をNiで置換させ、Liサイトの一部をKで置換さ
せたリチウムマンガン複合酸化物である。<Lithium-manganese composite oxide by precipitation aging method C> An aqueous solution in which Mn (NO 3 ) 2 and Ni (NO 3 ) 2 are dissolved and an aqueous solution of H 2 O 2 in which LiOH and KOH are dissolved are mixed. To form a composite oxide precursor, and aged at a variety of temperatures to produce a lithium manganese composite in which a part of the Mn site was replaced by Ni and a part of the Li site was replaced by K. It is an oxide.
【0044】まず、0.3MのMn(NO3)2水溶液と
0.3MのNi(NO3)2水溶液とをMn:Niがモル
比で19:1となるように混合した硝酸塩水溶液を10
0ml調製した。次いで、0.6MのLiOH/3wt
%H2O2水溶液180mlと0.6MのKOH/3wt
%H2O2水溶液20mlを混合させて水酸化物H2O2水
溶液を200ml調製した。上記硝酸塩水溶液と水酸化
物H2O2水溶液とを混合して混合溶液とし、スタラーピ
ースを用いて激しく攪拌させつつ5分間反応させて、組
成式(Li0.9K0.1)0.6Mn0.95Ni0.05O2・0.5
H2Oで表される層状岩塩構造の複合酸化物前駆体を析
出させた。次いで、この前駆体を析出後の混合溶液ごと
テフロンで内張りした容器に入れ、上記析出熟成法Aの
場合と同様、室温および50℃〜200℃の範囲の各種
温度で、2日間かけて熟成させ、その後、濾別、水洗、
乾燥させて各種リチウムマンガン複合酸化物を得た。そ
してこれらを析出熟成法Cによるリチウムマンガン複合
酸化物とした。First, an aqueous nitrate solution was prepared by mixing a 0.3 M aqueous solution of Mn (NO 3 ) 2 and a 0.3 M aqueous solution of Ni (NO 3 ) 2 so that the molar ratio of Mn: Ni was 19: 1.
0 ml was prepared. Then, 0.6M LiOH / 3wt
% H 2 O 2 aqueous solution 180ml and 0.6M KOH / 3wt
20 ml of a 20% aqueous solution of H 2 O 2 was mixed to prepare 200 ml of an aqueous solution of hydroxide H 2 O 2 . The aqueous nitrate solution and the aqueous hydroxide H 2 O 2 solution are mixed to form a mixed solution, and the mixture is reacted for 5 minutes with vigorous stirring using a stirrer piece to obtain a composition formula (Li 0.9 K 0.1 ) 0.6 Mn 0.95 Ni 0.05 O 2・ 0.5
A composite oxide precursor having a layered rock salt structure represented by H 2 O was precipitated. Next, this precursor is placed in a container lined with Teflon together with the mixed solution after deposition, and aged at room temperature and various temperatures in the range of 50 ° C. to 200 ° C. for 2 days as in the case of the above-mentioned precipitation aging method A. , Followed by filtration, washing with water,
By drying, various lithium manganese composite oxides were obtained. And these were made into the lithium manganese composite oxide by the precipitation aging method C.
【0045】〈固相反応法Aによるリチウムマンガン複
合酸化物〉上記析出熟成法によるものと比較すべく、従
来の固相反応法によって製造したもので、Mnサイト、
Liサイトのいずれもを置換させていないスピネル構造
のリチウムマンガン複合酸化物である。Mn2O3とLi
OHとを、Mn:Liがモル比で2:1.02となるよ
うで、自動乳鉢を用いて充分に混合し、この混合物を、
空気中において800℃の温度で6時間焼成することに
より製造した。このリチウムマンガン複合酸化物は組成
式LiMn2O4で表されるスピネル構造のものとなって
いる。<Lithium-manganese composite oxide by solid-phase reaction method A> A lithium-manganese composite oxide produced by a conventional solid-phase reaction method and compared with the one obtained by the above-mentioned precipitation ripening method,
This is a lithium manganese composite oxide having a spinel structure in which none of the Li sites are substituted. Mn 2 O 3 and Li
OH was sufficiently mixed using an automatic mortar so that the molar ratio of Mn: Li was 2: 1.02, and this mixture was
It was manufactured by firing in air at a temperature of 800 ° C. for 6 hours. This lithium manganese composite oxide has a spinel structure represented by a composition formula LiMn 2 O 4 .
【0046】〈固相反応法Bによるリチウムマンガン複
合酸化物〉上記析出熟成法によるものと比較すべく、従
来の固相反応法によって製造したもので、Mnサイトの
一部をNiで置換させたスピネル構造のリチウムマンガ
ン複合酸化物である。Mn2O3とNi(OH)2とLi
OHとを、Mn:Ni:Liがモル比で1.95:0.
05:1〜1.8:0.2:1となるように混合し、こ
の種々の混合物を、空気中において800℃の温度で6
時間焼成することにより種々の組成のものを製造した。
ちなみに、混合比がMn:Ni:Li=1.9:0.
1:1.02となる混合物を焼成したものが、組成式L
iMn1.9Ni0 .1O4で表されるスピネル構造リチウム
マンガン複合酸化物となっている。<Lithium-manganese composite oxide by solid-phase reaction method B> In order to compare with the above-mentioned one by the precipitation aging method, a lithium-manganese composite oxide was produced by a conventional solid-phase reaction method, and a part of the Mn site was replaced with Ni. It is a lithium manganese composite oxide having a spinel structure. Mn 2 O 3 , Ni (OH) 2 and Li
OH and Mn: Ni: Li in a molar ratio of 1.95: 0.
05: 1 to 1.8: 0.2: 1, and the various mixtures were mixed in air at 800 ° C. for 6 hours.
By firing for hours, various compositions were manufactured.
Incidentally, the mixing ratio is Mn: Ni: Li = 1.9: 0.
A mixture obtained by sintering a mixture of 1: 1.02 has a composition formula of L
and has a spinel structure lithium manganese composite oxide represented by iMn 1.9 Ni 0 .1 O 4.
【0047】〈析出熟成法によるリチウムマンガン複合
酸化物の結晶構造〉上記析出熟成法Aによって製造され
熟成温度の異なる種々のリチウムマンガン複合酸化物に
対して、X線回折分析を行うことにより、その結晶構造
を確認した。熟成温度が室温のものは、スピネル構造L
iMn2O4がほとんど生成されていない。熟成温度が5
0℃のものは、スピネル構造LiMn2O4の他に、未反
応の層状岩塩構造Li0.6MnO2・0.5H2Oが残存
している。また、熟成温度が200℃のものは、スピネ
ル構造LiMn2O4の他に、層状岩塩構造LiMnO 2
が副生している。これらに対して、熟成温度が70℃〜
150℃の範囲ものは、スピネル構造LiMn2O4の単
一相となっていることが確認できた。<Lithium manganese composite by precipitation aging method>
Crystal structure of oxide> produced by the above-mentioned precipitation aging method A
For various lithium manganese composite oxides with different aging temperatures
By conducting X-ray diffraction analysis, the crystal structure
It was confirmed. When the aging temperature is room temperature, the spinel structure L
iMnTwoOFourIs almost never generated. Aging temperature is 5
At 0 ° C., the spinel structure LiMnTwoOFourOther than
Layered rock salt structure Li0.6MnOTwo・ 0.5HTwoO remains
are doing. If the aging temperature is 200 ° C,
Structure LiMnTwoOFourIn addition, the layered rock salt structure LiMnO Two
Is a by-product. On the other hand, the aging temperature is 70 ° C.
In the range of 150 ° C., the spinel structure LiMnTwoOFourSimply
It was confirmed that they were in one phase.
【0048】同様に、上記析出熟成法Bによって製造さ
れ熟成温度の異なる種々のリチウムマンガン複合酸化物
に対しても、X線回折分析を行うことにより、その結晶
構造を確認した。Mn(NO3)2水溶液と0.3MのN
i(NO3)2水溶液とをMn:Niがモル比で19:1
となるように混合した水溶液を用いたものから製造した
リチウムマンガン複合酸化物について言えば、熟成温度
が室温の場合は、スピネル構造LiMn1.9Ni0.1O4
がほとんど生成されていない。熟成温度が50℃のもの
は、スピネル構造LiMn1.9Ni0.1O4の他に、未反
応の層状岩塩構造Li0.6Mn0.95Ni0.05O2・0.4
H2Oが残存している。析出熟成法Aの場合と異なり、
熟成温度が70℃〜200℃の範囲のものは、スピネル
構造LiMn1.9Ni0.1O4の単一相となっており、焼
成温度200℃の場合でも、層状岩塩構造LiMn0.95
Ni0.05O2は副生していないことが確認できた。析出
熟成法Aの場合と熟成温度200℃における結果が異な
るのは、上述したように、Ni置換によりMn4+が発生
し、スピネル構造が安定したためためであると考えられ
る。Similarly, X-ray diffraction analysis was performed on various lithium manganese composite oxides produced by the above-mentioned precipitation ripening method B and having different ripening temperatures to confirm their crystal structures. Mn (NO 3 ) 2 aqueous solution and 0.3M N
The i (NO 3 ) 2 aqueous solution was mixed with a molar ratio of Mn: Ni of 19: 1.
In the case of a lithium manganese composite oxide produced from an aqueous solution mixed such that the ripening temperature is room temperature, the spinel structure LiMn 1.9 Ni 0.1 O 4
Is almost never generated. Those having an aging temperature of 50 ° C. have an unreacted layered rock salt structure Li 0.6 Mn 0.95 Ni 0.05 O 2 .0.4 in addition to the spinel structure LiMn 1.9 Ni 0.1 O 4.
H 2 O remains. Unlike the case of precipitation aging method A,
Those having an aging temperature in the range of 70 ° C. to 200 ° C. have a single phase of spinel structure LiMn 1.9 Ni 0.1 O 4 , and even when the sintering temperature is 200 ° C., the layered rock salt structure LiMn 0.95
It was confirmed that Ni 0.05 O 2 was not produced as a by-product. It is considered that the reason why the result at the aging temperature of 200 ° C. is different from that in the case of the precipitation aging method A is that Mn 4+ is generated by Ni substitution and the spinel structure is stabilized as described above.
【0049】Mn(NO3)2水溶液と0.3MのNi
(NO3)2水溶液とをMn:Niがモル比で18:2と
なるように混合した水溶液を用いたものから製造した析
出熟成法Bのリチウムマンガン複合酸化物についても、
同様の結果が得られることが確認できた。なお、生成し
たスピネル構造のものは、組成式LiMn1.8Ni0.2O
4で表されるものであった。さらに、析出熟成法Cによ
るリチウムマンガン複合酸化物についても、析出熟成法
Bの場合と同様の結果が得られ、この場合のスピネル構
造のものは、組成式Li0.9K0.1Mn1.8Ni0.2O4で
表されるものであった。Mn (NOThree)TwoAqueous solution and 0.3M Ni
(NOThree)TwoThe aqueous solution was converted to Mn: Ni at a molar ratio of 18: 2.
Precipitation produced from using mixed aqueous solutions
Regarding the lithium manganese composite oxide of the ripening method B,
It was confirmed that similar results were obtained. In addition, generate
In the spinel structure, the composition formula is LiMn.1.8Ni0.2O
FourWas represented by Furthermore, according to the precipitation aging method C
Lithium manganese composite oxide
The same result as in the case of B was obtained, and the spinel structure in this case was obtained.
Is made of the composition formula Li0.9K0.1Mn1.8Ni0.2OFourso
Was represented.
【0050】参考までに、析出熟成法Aで得られたリチ
ウムマンガン複合酸化物であって、熟成温度が室温、5
0℃、80℃、120℃、200℃のものの、X線回折
分析における回折チャートを図1示す。また、析出熟成
法Bで得られたリチウムマンガン複合酸化物であって、
Mn(NO3)2水溶液と0.3MのNi(NO3)2水溶
液とをMn:Niがモル比で19:1となるように混合
した水溶液を用いたものから製造し、熟成温度が80
℃、200℃のものの、X線回折分析における回折チャ
ートを図2示す。なお、図1において、斜線で示した回
折ピークは、スピネル構造LiMn2O4の回折ピークで
ある。さらに、析出熟成法AないしCにおいて、熟成温
度と製造されるリチウム複合酸化物の組成および結晶構
造との関係を、代表的な熟成温度である50℃、80
℃、200℃の場合について、下記表1にまとめて示
す。For reference, a lithium manganese composite oxide obtained by the precipitation aging method A, wherein the aging temperature is room temperature, 5
FIG. 1 shows a diffraction chart of X-ray diffraction analysis at 0 ° C., 80 ° C., 120 ° C., and 200 ° C. Further, the lithium manganese composite oxide obtained by the precipitation aging method B,
An Mn (NO 3 ) 2 aqueous solution and a 0.3 M Ni (NO 3 ) 2 aqueous solution are produced from an aqueous solution obtained by mixing Mn: Ni at a molar ratio of 19: 1, and the ripening temperature is 80%.
FIG. 2 shows a diffraction chart of X-ray diffraction analysis at 200 ° C. and 200 ° C. In FIG. 1, the hatched diffraction peak is the diffraction peak of the spinel structure LiMn 2 O 4 . Further, in the precipitation aging methods A to C, the relationship between the aging temperature and the composition and crystal structure of the lithium composite oxide to be produced was evaluated by examining typical aging temperatures of 50 ° C. and 80 ° C.
Table 1 below shows the results for the cases of 200C and 200C.
【0051】[0051]
【表1】 [Table 1]
【0052】次に、析出熟成法A、析出熟成法Bによっ
て得られたスピネル構造リチウムマンガン複合酸化物
と、固相反応法A、固相反応法Bによって得られたスピ
ネル構造リチウムマンガン複合酸化物とにおいて、Mn
サイトのNiでの置換割合の変化よる格子定数の値の変
化について比較した。図3にこの結果を示す。Mnサイ
トを置換していないおよびその一部をNiで置換したス
ピネル構造リチウムマンガン複合酸化物は、組成式Li
Mn2-yNiyO4で一般化でき、この組成式中のyの値
を置換割合とすることができる。析出熟成法によるもの
についても、また、固相反応法によるものについても、
置換割合yが大きくなるにつれて、格子定数aの値は直
線的に小さくなっている。そしてさらに判ることは、製
造方法の違いによっても、格子定数aの値が異ならない
ことである。したがってこのことからも、本発明の製造
方法が採用する析出熟成法は、100℃以下という比較
的低温処を行うにもかかわらず、500℃以上という高
温で処理する従来の固相反応法と同様に、結晶性のよい
スピネル構造リチウムマンガン複合酸化物を製造できる
ことが確認できる。Next, the spinel-structured lithium manganese composite oxide obtained by the precipitation aging method A and the precipitation aging method B, and the spinel-structured lithium manganese composite oxide obtained by the solid-state reaction method A and the solid-state reaction method B And Mn
A comparison was made of the change in the value of the lattice constant due to the change in the substitution ratio of Ni at the site. FIG. 3 shows the result. A spinel-structured lithium manganese composite oxide in which the Mn site is not substituted and a part of which is substituted by Ni has a composition formula of Li
It can be generalized to Mn 2-y Ni y O 4 , and the value of y in this composition formula can be used as the substitution ratio. About the thing by the precipitation aging method, and also about the thing by the solid phase reaction method,
As the substitution ratio y increases, the value of the lattice constant a decreases linearly. Further, it is clear that the value of the lattice constant a does not differ depending on the manufacturing method. Therefore, from this, the precipitation ripening method adopted by the production method of the present invention is the same as the conventional solid-phase reaction method in which the treatment is performed at a high temperature of 500 ° C. or higher, despite performing a relatively low temperature treatment of 100 ° C. or lower. Furthermore, it can be confirmed that a lithium-manganese composite oxide having a spinel structure having good crystallinity can be produced.
【0053】〈正極活物質としての評価〉上記析出熟成
法によるリチウムマンガン複合酸化物と固相反応法によ
るリチウムマンガン複合酸化物を正極活物質として用
い、金属リチウムを負極に用いたコイン型リチウム二次
電池を作製した。それぞれのリチウム二次電池に対して
充放電サイクル試験を行い、初期放電容量、容量維持率
について確認し、本発明の製造方法が採用する析出熟成
法によるリチウムマンガン複合酸化物の正極活物質とし
ての性能を評価した。<Evaluation as Positive Electrode Active Material> A coin-type lithium secondary battery using a lithium manganese composite oxide prepared by the above-described precipitation ripening method and a lithium manganese composite oxide prepared by a solid phase reaction method as a positive electrode active material and metallic lithium as a negative electrode was used. A secondary battery was manufactured. A charge / discharge cycle test was performed on each lithium secondary battery, the initial discharge capacity and the capacity retention were confirmed, and the lithium manganese composite oxide was used as a positive electrode active material of a lithium manganese composite oxide by a precipitation aging method employed in the production method of the present invention. The performance was evaluated.
【0054】コイン型リチウム二次電池の正極は、上記
それぞれのリチウムマンガン複合酸化物粉末の70重量
部に、導電材としてのアセチレンブラックを25重量
部、結着剤としてのポリフッ化ビニリデンを5重量部混
合し、2t/cm2の圧力で加圧成形したのち、真空
中、200℃の温度で熱処理して作製した。非水電解液
には、エチレンカーボネートとジエチルカーボネートと
を体積比1:1に混合した混合溶媒に、LiPF6を1
Mの濃度で溶解させたものを用いた。In the positive electrode of the coin-type lithium secondary battery, 70 parts by weight of the respective lithium manganese composite oxide powder, 25 parts by weight of acetylene black as a conductive material, and 5 parts by weight of polyvinylidene fluoride as a binder were used. The mixture was partially mixed, press-molded at a pressure of 2 t / cm 2 , and then heat-treated at a temperature of 200 ° C. in a vacuum to produce the film. The non-aqueous electrolyte contains LiPF 6 in a mixed solvent of ethylene carbonate and diethyl carbonate in a volume ratio of 1: 1.
M dissolved at a concentration of M was used.
【0055】作製したそれぞれのリチウム二次電池に対
して行った充放電サイクル試験の条件は、60℃の温度
下、電流密度1mA/cm2で終止電圧4.2Vまで充
電した後、10分間休止させ、次いで電流密度1mA/
cm2で終止電圧3.0Vまで放電した後、10分間休
止させる工程を1サイクルとするもので、このサイクル
を50サイクル以上繰り返すものとした。各電池の正極
活物質単位重量あたりの放電容量および50サイクル後
の容量維持率(50サイクル目の放電容量/初期放電容
量)を求めた。下記表2にこの結果の一例を示す。な
お、表2には、析出熟成法によるリチウムマンガン複合
酸化物を用いた二次電池については熟成温度が80℃お
よび200℃のものを掲げた。なお析出熟成法B、固相
反応法Bのものについては、MnサイトのNiでの置換
割合つまり組成式中のyの値が0.1となるもののみを
掲げてある。The conditions of the charge / discharge cycle test performed on each of the manufactured lithium secondary batteries were as follows: at a temperature of 60 ° C., a current density of 1 mA / cm 2 , a charge to a final voltage of 4.2 V, and a 10-minute pause. And then a current density of 1 mA /
After discharging to a final voltage of 3.0 V in cm 2 , a step of resting for 10 minutes was defined as one cycle, and this cycle was repeated 50 times or more. The discharge capacity per unit weight of the positive electrode active material and the capacity retention rate after 50 cycles (discharge capacity at 50th cycle / initial discharge capacity) of each battery were determined. Table 2 below shows an example of this result. Table 2 shows the secondary batteries using the lithium manganese composite oxide prepared by the precipitation aging method with aging temperatures of 80 ° C and 200 ° C. In the case of the precipitation ripening method B and the solid-phase reaction method B, only those in which the substitution ratio of Mn sites by Ni, that is, the value of y in the composition formula is 0.1 are listed.
【0056】[0056]
【表2】 [Table 2]
【0057】上記表2から判るように、固相反応法によ
るものを用いた二次電池と析出熟成法によるものを用い
た二次電池との間で、初期放電容量、容量維持率に大差
はなく、析出熟成法によるリチウムマンガン複合酸化物
は、良好な正極活物質となり得ることが確認できる。ま
た、MnサイトのNiによる置換、LiサイトのKによ
る置換によって、初期放電容量は低下するものの容量維
持率は高くなり、サイクル特性の良好なより実用的な二
次電池を構成できる正極活物質となり得ることが確認で
きる。この置換による効果についても、固相反応法によ
るものと析出熟成法によるものとの間に特別な差異は見
られていない。As can be seen from Table 2, there is a large difference in the initial discharge capacity and the capacity retention between the secondary battery using the solid-state reaction method and the secondary battery using the precipitation aging method. However, it can be confirmed that the lithium manganese composite oxide obtained by the precipitation aging method can be a good positive electrode active material. In addition, the replacement of the Mn site by Ni and the replacement of the Li site by K lowers the initial discharge capacity but increases the capacity retention rate, and becomes a positive electrode active material that can constitute a more practical secondary battery with good cycle characteristics. It can be confirmed that it is obtained. Regarding the effect of this substitution, no special difference is found between the solid phase reaction method and the precipitation ripening method.
【0058】ただし、析出熟成法Aによる熟成温度20
0℃のものは、本発明の製造方法における好適熟成温度
から外れた温度で熟成されたものであり、製造されたリ
チウムマンガン複合酸化物中に、層状岩塩構造LiMn
O2の相が副生している。そのため、50サイクル後の
容量維持率が75%と低い値となっている。したがって
このことから、サイクル特性の良好な二次電池を構成で
きるリチウムマンガン複合酸化物を製造するためには、
上記好適熟成温度範囲で熟成させるのが望ましいことが
確認できる。However, the aging temperature by the precipitation aging method A is 20
Those having a temperature of 0 ° C. have been aged at a temperature outside the preferred aging temperature in the production method of the present invention, and have a layered rock salt structure LiMn in the produced lithium manganese composite oxide.
O 2 phase is by-produced. Therefore, the capacity retention rate after 50 cycles is a low value of 75%. Therefore, from this, in order to produce a lithium manganese composite oxide that can constitute a secondary battery having good cycle characteristics,
It can be confirmed that it is desirable to ripen in the above preferable ripening temperature range.
【0059】次に、本発明の製造方法である析出熟成法
が、固相反応法と比較して、結晶全体の組成の均一性に
より優れたリチウムマンガン複合酸化物を製造できるこ
とを確認すべく、それぞれの方法によるリチウムマンガ
ン複合酸化物を正極活物質に用いた二次電池の充放電特
性曲線を作製した。比較する二次電池の1つは、上記析
出熟成法Bによる熟成温度80℃のものを用いた二次電
池であり、もう1つは、固相反応法Bによるものを用い
た二次電池である。なお、使用したリチウムマンガン複
合酸化物は、両者とも、全体組成がLiMn1.9Ni0.1
O4で表されるスピネル構造のものである。両者の充放
電特性曲線を図4に示す。Next, in order to confirm that the precipitation aging method, which is the production method of the present invention, can produce a lithium manganese composite oxide which is more excellent in the uniformity of the composition of the whole crystal as compared with the solid phase reaction method. A charge / discharge characteristic curve of a secondary battery using a lithium manganese composite oxide according to each method as a positive electrode active material was prepared. One of the secondary batteries to be compared is a secondary battery using an aging temperature of 80 ° C. by the above-mentioned precipitation aging method B, and the other is a secondary battery using an aging temperature by the solid phase reaction method B. is there. The lithium manganese composite oxide used had an overall composition of LiMn 1.9 Ni 0.1
It has a spinel structure represented by O 4 . FIG. 4 shows the charge / discharge characteristic curves of the two.
【0060】図4から判るように、固相反応法によるも
のは、充電側、放電側とも、電池の端子間電圧が、時間
の経過につれ階段状に変化している。これに対して、析
出熟成法によるものは充電側、放電側とも、電池の端子
間電圧が直線的に変化している。固相反応法による場合
は、出発原料を極めて均一な状態に混合することが難し
く、置換元素源とな材料を添加する場合はさらに困難と
なる。したがって、固相反応法によるものの場合は、置
換元素であるNiが結晶中に偏析した状態になってお
り、このために、充放電に伴い結晶が相転移し、充放電
特性曲線が階段状になるものと考えられる。これに対し
て、直線的に変化する析出熟成法によるものの場合は、
Niの偏析といった現象が発生していないと考えられ
る。つまり、本発明の製造方法の析出工程は、液相ので
の反応であるため、出発原料となる物質の混合状態を極
めて均一なものにできるからである。この結果から、本
発明の製造方法は、結晶全体の組成の均一性により優れ
たリチウムマンガン複合酸化物を、容易に製造できる方
法であることが確認できる。As can be seen from FIG. 4, in the case of the solid-state reaction method, the voltage between the terminals of the battery changes stepwise over time on both the charging side and the discharging side. On the other hand, according to the precipitation aging method, the voltage between the terminals of the battery changes linearly on both the charging side and the discharging side. In the case of the solid-phase reaction method, it is difficult to mix the starting materials in an extremely uniform state, and it is more difficult to add a material serving as a substitution element source. Therefore, in the case of the solid-phase reaction method, Ni as a substitution element is segregated in the crystal, and the crystal undergoes a phase transition with charge / discharge, and the charge / discharge characteristic curve changes stepwise. It is considered to be. In contrast, in the case of the precipitation aging method that changes linearly,
It is considered that a phenomenon such as Ni segregation did not occur. That is, since the precipitation step of the production method of the present invention is a reaction in a liquid phase, the mixed state of the starting materials can be made extremely uniform. From these results, it can be confirmed that the production method of the present invention is a method that can easily produce a lithium manganese composite oxide having more excellent composition uniformity of the whole crystal.
【0061】[0061]
【発明の効果】本発明のリチウム二次電池正極活物質用
リチウムマンガン複合酸化物の製造方法は、マンガン源
あるいはマンガンおよびマンガンサイトを置換可能な他
元素源となる硝酸塩水溶液と、リチウム源またはリチウ
ムおよびリチウムサイトを置換可能なアルカリ金属元素
源となる水酸化物のH2O2水溶液とを混合し、溶液反応
によって、層状岩塩構造の複合酸化物前駆体を析出させ
る析出工程と、析出した前駆体を比較的低温度中に保持
して熟成させ、結晶構造を層状岩塩構造からスピネル構
造へ転移させる熟成工程とから構成される。The method for producing a lithium-manganese composite oxide for a lithium secondary battery positive electrode active material according to the present invention comprises a nitrate aqueous solution serving as a manganese source or another element source capable of replacing manganese and manganese sites; And an aqueous solution of a hydroxide serving as a source of an alkali metal element capable of replacing a lithium site with a H 2 O 2 aqueous solution of a hydroxide, and performing a solution reaction to precipitate a composite oxide precursor having a layered rock salt structure; An aging step in which the body is kept at a relatively low temperature for aging and the crystal structure is changed from a layered rock salt structure to a spinel structure.
【0062】このような構成としたことにより、本発明
の製造方法は、結晶全体の組成の均一性に優れたスピネ
ル構造リチウムマンガン複合酸化物を、比較的低温度の
処理によって、低コストにかつ簡便に製造できる方法と
なる。By adopting such a constitution, the production method of the present invention can produce a spinel-structured lithium manganese composite oxide having excellent uniformity in the composition of the whole crystal at a relatively low temperature and at a low cost. This is a method that can be easily manufactured.
【図1】 本発明の製造方法である析出熟成法によって
製造されたリチウムマンガン複合酸化物のX線回折チャ
ートを示す。FIG. 1 shows an X-ray diffraction chart of a lithium manganese composite oxide produced by a precipitation aging method that is a production method of the present invention.
【図2】 本発明の製造方法である析出熟成法によって
製造され、Mnサイトの一部をNiで置換させたリチウ
ムマンガン複合酸化物のX線回折チャートを示す。FIG. 2 shows an X-ray diffraction chart of a lithium manganese composite oxide produced by a precipitation aging method, which is a production method of the present invention, in which a part of Mn sites has been substituted by Ni.
【図3】 析出熟成法および固相反応法のそれそれの方
法によって製造されたリチウムマンガン複合酸化物の、
MnサイトのNiによる置換割合の変化に対する格子定
数の変化を示す。FIG. 3 shows a lithium manganese composite oxide produced by a precipitation ripening method and a solid phase reaction method.
The change of the lattice constant with respect to the change of the substitution ratio of Mn site by Ni is shown.
【図4】 析出熟成法および固相反応法のそれそれの方
法によって製造され、Mnサイトの一部をNiで置換さ
せたリチウムマンガン複合酸化物の、充放電特性曲線を
示す。FIG. 4 shows a charge / discharge characteristic curve of a lithium manganese composite oxide produced by a precipitation ripening method and a solid phase reaction method, in which a part of the Mn site is substituted by Ni.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) H01M 4/58 H01M 4/58 10/40 10/40 Z Fターム(参考) 4G002 AA06 AA10 AB02 AE05 4G048 AA04 AB02 AC06 AD06 AE07 5H003 AA08 BA00 BA03 BB01 BB04 BB05 BC06 BD00 BD01 BD03 5H014 AA02 BB01 BB05 BB06 BB08 CC01 EE08 EE10 5H029 AJ14 AK03 AK19 AL01 AL06 AL12 AM03 AM04 AM05 AM07──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) H01M 4/58 H01M 4/58 10/40 10/40 Z F-term (Reference) 4G002 AA06 AA10 AB02 AE05 4G048 AA04 AB02 AC06 AD06 AE07 5H003 AA08 BA00 BA03 BB01 BB04 BB05 BC06 BD00 BD01 BD03 5H014 AA02 BB01 BB05 BB06 BB08 CC01 EE08 EE10 5H029 AJ14 AK03 AK19 AL01 AL06 AL12 AM03 AM04 AM05 AM07
Claims (8)
o、Cr、Fe、Al、Tiから選ばれる1種以上であ
ってすくなくともMnを含む、mはMeの価数に応じた
値)を水に溶解させた硝酸塩水溶液と、AOH(Aはア
ルカリ金属から選ばれる1種以上であって少なくともL
iを含む)をH2O2水溶液に溶解させた水酸化物H2O2
水溶液とを混合させて混合溶液とし、該混合溶液中に組
成式AxMeO2・nH2O(0<x≦1、0.1≦n≦
1)で表される層状岩塩構造の複合酸化物前駆体を析出
させる析出工程と、 析出後の前記混合溶液中で前記複合酸化物前駆体を熟成
させ、組成式AMe2O4で表されるスピネル構造のリチ
ウムマンガン複合酸化物を得る熟成工程と、 を含んでなるリチウム二次電池正極活物質用リチウムマ
ンガン複合酸化物の製造方法。1. Me (NO 3 ) m (Me is Mn, Ni, C
a nitrate aqueous solution in which at least one selected from the group consisting of o, Cr, Fe, Al, and Ti and containing at least Mn, where m is a value corresponding to the valency of Me, is dissolved in water; At least one member selected from the group consisting of at least L
hydroxides containing i) was dissolved in aqueous solution of H 2 O 2 H 2 O 2
An aqueous solution is mixed to form a mixed solution, and a composition formula A x MeO 2 .nH 2 O (0 <x ≦ 1, 0.1 ≦ n ≦
A precipitation step of precipitating a composite oxide precursor having a layered rock salt structure represented by 1), and aging the composite oxide precursor in the mixed solution after deposition, represented by a composition formula AMe 2 O 4 A method for producing a lithium manganese composite oxide for a lithium secondary battery positive electrode active material, comprising: an aging step of obtaining a lithium manganese composite oxide having a spinel structure.
はLiのみからなり、 前記複合酸化物前駆体は組成式LixMnO2・nH2O
で表され、かつ前記リチウムマンガン複合酸化物は組成
式LiMn2O4で表され、 前記熟成工程の熟成温度は50℃を超え200℃未満で
ある請求項1に記載のリチウム二次電池正極活物質用リ
チウムマンガン複合酸化物の製造方法。2. The method according to claim 1, wherein the Me comprises only Mn and the A
Is composed only of Li, and the composite oxide precursor has a composition formula of Li x MnO 2 .nH 2 O
The lithium manganese composite oxide is represented by a composition formula LiMn 2 O 4 , and the aging temperature in the aging step is higher than 50 ° C. and lower than 200 ° C. 2. Method for producing lithium manganese composite oxide for substances.
m'(Me'はNi、Co、Cr、Fe、Al、Tiから
選ばれる1種以上、m'はMe'の価数に応じた値)とを
MnとMe'とのモル比が2−y:yとなるように溶解
して調製され、 前記複合酸化物前駆体は組成式LixMn1-y/2Me'y/2
O2・nH2Oで表され、かつ前記リチウムマンガン複合
酸化物は組成式LiMn2-yMe'yO4で表され、 前記
熟成工程の熟成温度は50℃を超え300℃未満である
請求項1に記載のリチウム二次電池正極活物質用リチウ
ムマンガン複合酸化物の製造方法。ただし、0<y≦
0.5とする。3. The method according to claim 1, wherein A comprises only Li, and the nitrate aqueous solution contains Mn (NO 3 ) 2 and Me ′ (NO 3 ).
m ′ (Me ′ is at least one selected from Ni, Co, Cr, Fe, Al and Ti, m ′ is a value corresponding to the valence of Me ′) and the molar ratio between Mn and Me ′ is 2- y: y is prepared by dissolving so that the composite oxide precursor has a composition formula of Li x Mn 1-y / 2 Me ′ y / 2
O 2 · nH 2 O, wherein the lithium manganese composite oxide is represented by a composition formula LiMn 2-y Me ′ y O 4 , wherein the aging temperature in the aging step is higher than 50 ° C. and lower than 300 ° C. Item 4. The method for producing a lithium manganese composite oxide for a lithium secondary battery positive electrode active material according to Item 1. However, 0 <y ≦
0.5.
はLiを除くアルカリ金属から選ばれる1種以上)とを
LiとA'とのモル比が1−z:zとなるように溶解し
て調製され、 前記複合酸化物前駆体は組成式(Li1-zA'z)xMnO
2・nH2Oで表され、かつ前記リチウムマンガン複合酸
化物は組成式Li1-zA'zMn2O4で表され、 前記熟成工程の熟成温度は50℃を超え200℃未満で
ある請求項1に記載のリチウム二次電池正極活物質用リ
チウムマンガン複合酸化物の製造方法。ただし、0<z
≦0.3とする。4. The Me comprises only Mn, and the aqueous solution of hydroxide H 2 O 2 comprises LiOH and A′OH (A ′).
Is prepared by dissolving at least one selected from alkali metals excluding Li) such that the molar ratio of Li and A ′ is 1-z: z, and the composite oxide precursor has a composition formula (Li 1-z A ' z ) x MnO
2 · nH 2 O, and the lithium manganese composite oxide is represented by a composition formula Li 1-z A ′ z Mn 2 O 4 , and the aging temperature in the aging step is higher than 50 ° C. and lower than 200 ° C. A method for producing a lithium manganese composite oxide for a lithium secondary battery positive electrode active material according to claim 1. However, 0 <z
≦ 0.3.
Me'(NO3)m'(Me'はNi、Co、Cr、Fe、
Al、Tiから選ばれる1種以上、m'はMe'の価数に
応じた値)とをMnとMe'とのモル比が2−y:yと
なるように溶解して調製され、 前記水酸化物H2O2水溶液は、LiOHとA'OH(A'
はLiを除くアルカリ金属から選ばれる1種以上)とを
LiとA'とのモル比が1−z:zとなるように溶解し
て調製され、 前記複合酸化物前駆体は組成式(Li1-zA'z)xMn
1-y/2Me'y/2O2・nH 2Oで表され、かつ前記リチウ
ムマンガン複合酸化物は組成式Li1-zA'zMn2- yM
e'yO4で表され前記熟成工程の熟成温度は50℃を超
え300℃未満である請求項1に記載のリチウム二次電
池正極活物質用リチウムマンガン複合酸化物の製造方
法。ただし、0<y≦0.5、0<z≦0.3とする。5. The method according to claim 1, wherein the nitrate aqueous solution contains Mn (NOThree)TwoWhen
Me '(NOThree)m '(Me ′ is Ni, Co, Cr, Fe,
At least one selected from Al and Ti, m 'is a valence of Me'
And the molar ratio between Mn and Me ′ is 2-y: y and
The hydroxide H is prepared by dissolvingTwoOTwoThe aqueous solution is LiOH and A'OH (A '
Is one or more selected from alkali metals except Li) and
Li was dissolved so that the molar ratio of Li and A ′ became 1-z: z.
The composite oxide precursor is prepared by the composition formula (Li1-zA 'z)xMn
1-y / 2Me 'y / 2OTwo・ NH TwoO, and said lithium
Mumanganese composite oxide has the composition formula Li1-zA 'zMn2- yM
e 'yOFourThe aging temperature of the aging step is higher than 50 ° C.
2. The lithium secondary battery according to claim 1, wherein the temperature is lower than 300 ° C.
Of Lithium-Manganese Composite Oxide for Pond Positive Electrode Active Material
Law. However, 0 <y ≦ 0.5 and 0 <z ≦ 0.3.
請求項5に記載のリチウム二次電池正極活物質用リチウ
ムマンガン複合酸化物の製造方法。6. The method for producing a lithium manganese composite oxide for a lithium secondary battery positive electrode active material according to claim 3, wherein Me ′ is Ni.
項5のいずれかに記載のリチウム二次電池正極活物質用
リチウムマンガン複合酸化物の製造方法。7. The method for producing a lithium manganese composite oxide for a lithium secondary battery positive electrode active material according to claim 4, wherein A ′ is K.
である請求項5に記載のリチウム二次電池正極活物質用
リチウムマンガン複合酸化物の製造方法。8. The method according to claim 8, wherein Me ′ is Ni and A ′ is K
The method for producing a lithium-manganese composite oxide for a positive electrode active material for a lithium secondary battery according to claim 5.
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|---|---|---|---|
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Family
ID=13661222
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|---|---|---|---|
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